US10717255B2 - Polymeric films and methods for making polymeric films - Google Patents

Polymeric films and methods for making polymeric films Download PDF

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Publication number
US10717255B2
US10717255B2 US15/341,103 US201615341103A US10717255B2 US 10717255 B2 US10717255 B2 US 10717255B2 US 201615341103 A US201615341103 A US 201615341103A US 10717255 B2 US10717255 B2 US 10717255B2
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United States
Prior art keywords
layer
film
psi
gsm
cavitated
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US15/341,103
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US20170129228A1 (en
Inventor
Jeffrey A. Middlesworth
Brooke D. Kitzmiller
Vadim G. Zaikov
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Berry Plastics Corp
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Priority to US15/341,103 priority Critical patent/US10717255B2/en
Assigned to BERRY PLASTICS CORPORATION reassignment BERRY PLASTICS CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: MIDDLESWORTH, JEFFREY A., ZAIKOV, Vadim G., KITZMILLER, Brooke D.
Publication of US20170129228A1 publication Critical patent/US20170129228A1/en
Assigned to CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH, BANK OF AMERICA reassignment CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH FIRST LIEN INTELLECTUAL PROPERTY SECURITY AGREEMENT Assignors: AVINTIV SPECIALTY MATERIALS INC., BERRY FILM PRODUCTS COMPANY, INC., BERRY GLOBAL FILMS, LLC, BERRY PLASTICS FILMCO, INC., BPREX HEALTHCARE PACKAGING INC., COVALENCE SPECIALTY ADHESIVES LLC, FIBERWEB, LLC, PLIANT, LLC, PRIME LABEL AND SCREEN INCORPORATED, ROLLPAK CORPORATION
Assigned to U.S. BANK NATIONAL ASSOCIATION, AS COLLATERAL AGENT reassignment U.S. BANK NATIONAL ASSOCIATION, AS COLLATERAL AGENT FIRST LIEN PATENT SECURITY AGREEMENT Assignors: AVINTIV SPECIALTY MATERIALS INC., BERRY FILM PRODUCTS COMPANY, INC., BERRY GLOBAL FILMS, LLC, BERRY GLOBAL, INC., BPREX HEALTHCARE PACKAGING INC., FIBERWEB, LLC, PLIANT, LLC, PRIME LABEL & SCREEN INCORPORATED, PRIME LABEL & SCREEN, INC., PROVIDENCIA USA, INC.
Assigned to CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH, BANK OF AMERICA, N.A. reassignment CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH FIRST LIEN INTELLECTUAL PROPERTY SECURITY AGREEMENT Assignors: AVINTIV SPECIALTY MATERIALS INC., BERRY FILM PRODUCTS COMPANY, INC., BERRY GLOBAL FILMS, LLC, BERRY PLASTICS FILMCO, INC., BPREX HEALTHCARE PACKAGING INC., COVALENCE SPECIALTY ADHESIVES LLC, FIBERWEB, LLC, PLIANT, LLC, PRIME LABEL AND SCREEN INCORPORATED, ROLLPAK CORPORATION
Assigned to U.S. BANK NATIONAL ASSOCIATION, AS COLLATERAL AGENT reassignment U.S. BANK NATIONAL ASSOCIATION, AS COLLATERAL AGENT FIRST LIEN PATENT SECURITY AGREEMENT Assignors: AVINTIV SPECIALTY MATERIALS INC., BERRY FILM PRODUCTS COMPANY, INC., BERRY GLOBAL FILMS, LLC, BERRY GLOBAL, INC., BPREX HEALTHCARE PACKAGING INC., FIBERWEB, LLC, PLIANT, LLC, PRIME LABEL & SCREEN INCORPORATED, PRIME LABEL & SCREEN, INC., PROVIDENCIA USA, INC.
Publication of US10717255B2 publication Critical patent/US10717255B2/en
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Assigned to U.S. BANK NATIONAL ASSOCIATION reassignment U.S. BANK NATIONAL ASSOCIATION FIRST LIEN PATENT SECURITY AGREEMENT Assignors: AVINTIV SPECIALTY MATERIALS INC., BERRY FILM PRODUCTS COMPANY, INC., BERRY GLOBAL FILMS, LLC, BERRY GLOBAL, INC., BPREX HEALTHCARE PACKAGING INC., FIBERWEB, LLC, LETICA CORPORATION, PLIANT, LLC, PRIME LABEL & SCREEN, INC., PRIME LABEL AND SCREEN INCORPORATED, PROVIDENCIA USA, INC.
Assigned to U.S. BANK NATIONAL ASSOCIATION reassignment U.S. BANK NATIONAL ASSOCIATION FIRST LIEN PATENT SECURITY AGREEMENT Assignors: AVINTIV SPECIALTY MATERIALS INC., BERRY FILM PRODUCTS COMPANY, INC., BERRY GLOBAL FILMS, LLC, BERRY GLOBAL, INC., BPREX HEALTHCARE PACKAGING INC., FIBERWEB, LLC, LETICA CORPORATION, PLIANT, LLC, PRIME LABEL & SCREEN, INC., PRIME LABEL AND SCREEN INCORPORATED, PROVIDENCIA USA, INC.
Assigned to U.S. BANK NATIONAL ASSOCIATION reassignment U.S. BANK NATIONAL ASSOCIATION CORRECTIVE ASSIGNMENT TO CORRECT THE LISTING OF PATENTS PREVIOUSLY RECORDED AT REEL: 054840 FRAME: 0047. ASSIGNOR(S) HEREBY CONFIRMS THE FIRST LIEN PATENT SECURITY AGREEMENT. Assignors: AVINTIV SPECIALTY MATERIALS INC., BERRY FILM PRODUCTS COMPANY, INC., BERRY GLOBAL FILMS, LLC, BERRY GLOBAL, INC., BPREX HEALTHCARE PACKAGING INC., FIBERWEB, LLC, LETICA CORPORATION, PLIANT, LLC, PRIME LABEL & SCREEN, INC., PRIME LABEL AND SCREEN INCORPORATED, PROVIDENCIA USA, INC.
Assigned to U.S. BANK NATIONAL ASSOCIATION reassignment U.S. BANK NATIONAL ASSOCIATION CORRECTIVE ASSIGNMENT TO CORRECT THE LISTING OF PATENTS PREVIOUSLY RECORDED ON REEL 055009 FRAME 0450. ASSIGNOR(S) HEREBY CONFIRMS THE FIRST LIEN PATENT SECURITY AGREEMENT. Assignors: AVINTIV SPECIALTY MATERIALS INC., BERRY FILM PRODUCTS COMPANY, INC., BERRY GLOBAL FILMS, LLC, BERRY GLOBAL, INC., BPREX HEALTHCARE PACKAGING INC., FIBERWEB, LLC, LETICA CORPORATION, PLIANT, LLC, PRIME LABEL & SCREEN, INC., PRIME LABEL AND SCREEN INCORPORATED, PROVIDENCIA USA, INC.
Assigned to U.S. BANK NATIONAL ASSOCIATION, AS COLLATERAL AGENT reassignment U.S. BANK NATIONAL ASSOCIATION, AS COLLATERAL AGENT SECURITY INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: AVINTIV SPECIALTY MATERIALS INC., BERRY FILM PRODUCTS COMPANY, INC., BERRY GLOBAL FILMS, LLC, BERRY GLOBAL, INC., BPREX HEALTHCARE PACKAGING INC., FIBERWEB, LLC, LETICA CORPORATION, PLIANT, LLC, PROVIDENCIA USA, INC.
Assigned to U.S. BANK NATIONAL ASSOCIATION reassignment U.S. BANK NATIONAL ASSOCIATION CORRECTIVE ASSIGNMENT TO CORRECT THE THE LISTING OF PATENTS PREVIOUSLY RECORDED AT REEL: 055009 FRAME: 0450. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Assignors: AVINTIV SPECIALTY MATERIALS INC., BERRY FILM PRODUCTS COMPANY, INC., BERRY GLOBAL FILMS, LLC, BERRY GLOBAL, INC., BPREX HEALTHCARE PACKAGING INC., FIBERWEB, LLC, LETICA CORPORATION, PLIANT, LLC, PRIME LABEL & SCREEN, INC., PRIME LABEL AND SCREEN INCORPORATED, PROVIDENCIA USA, INC.
Assigned to U.S. BANK NATIONAL ASSOCIATION reassignment U.S. BANK NATIONAL ASSOCIATION CORRECTIVE ASSIGNMENT TO CORRECT THE THE LISTING OF PATENTS PREVIOUSLY RECORDED AT REEL: 054840 FRAME: 0047. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Assignors: AVINTIV SPECIALTY MATERIALS INC., BERRY FILM PRODUCTS COMPANY, INC., BERRY GLOBAL FILMS, LLC, BERRY GLOBAL, INC., BPREX HEALTHCARE PACKAGING INC., FIBERWEB, LLC, LETICA CORPORATION, PLIANT, LLC, PRIME LABEL & SCREEN, INC., PRIME LABEL AND SCREEN INCORPORATED, PROVIDENCIA USA, INC.
Assigned to U.S. BANK TRUST COMPANY, NATIONAL ASSOCIATION reassignment U.S. BANK TRUST COMPANY, NATIONAL ASSOCIATION SECURITY INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: AVINTIV SPECIALTY MATERIALS INC., BERRY FILM PRODUCTS COMPANY, INC., BERRY GLOBAL FILMS, LLC, BERRY GLOBAL, INC., BPREX HEALTHCARE PACKAGING INC, FIBERWEB, LLC, LETICA CORPORATION, PLIANT, LLC, PRIME LABEL & SCREEN, INC., PRIME LABEL & SCREEN, INCORPORATED, PROVIDENCIA USA, INC.
Assigned to U.S. BANK NATIONAL ASSOCIATION reassignment U.S. BANK NATIONAL ASSOCIATION CORRECTIVE ASSIGNMENT TO CORRECT THE APPLICATION NUMBERS PREVIOUSLY RECORDED AT REEL: 055009 FRAME: 0450. ASSIGNOR(S) HEREBY CONFIRMS THE SECURITY AGREEMENT. Assignors: AVINTIV SPECIALTY MATERIALS INC., BERRY FILM PRODUCTS COMPANY, INC., BERRY GLOBAL FILMS, LLC, BERRY GLOBAL, INC., BPREX HEALTHCARE PACKAGING INC., FIBERWEB, LLC, LETICA CORPORATION, PLIANT, LLC, PRIME LABEL & SCREEN, INC., PRIME LABEL AND SCREEN INCORPORATED, PROVIDENCIA USA, INC.
Assigned to U.S. BANK NATIONAL ASSOCIATION, AS COLLATERAL AGENT reassignment U.S. BANK NATIONAL ASSOCIATION, AS COLLATERAL AGENT CORRECTIVE ASSIGNMENT TO CORRECT THE APPLICATION NUMBERS PREVIOUSLY RECORDED AT REEL: 056759 FRAME: 0001. ASSIGNOR(S) HEREBY CONFIRMS THE SECURITY INTEREST. Assignors: AVINTIV SPECIALTY MATERIALS INC., BERRY FILM PRODUCTS COMPANY, INC., BERRY GLOBAL FILMS, LLC, BERRY GLOBAL, INC., BPREX HEALTHCARE PACKAGING INC., FIBERWEB, LLC, LETICA CORPORATION, PLIANT, LLC, PROVIDENCIA USA, INC.
Assigned to U.S. BANK NATIONAL ASSOCIATION reassignment U.S. BANK NATIONAL ASSOCIATION CORRECTIVE ASSIGNMENT TO CORRECT THE APPLICATION NUMBERS PREVIOUSLY RECORDED AT REEL: 055616 FRAME: 0527. ASSIGNOR(S) HEREBY CONFIRMS THE SECURITY AGREEMENT. Assignors: AVINTIV SPECIALTY MATERIALS INC., BERRY FILM PRODUCTS COMPANY, INC., BERRY GLOBAL FILMS, LLC, BERRY GLOBAL, INC., BPREX HEALTHCARE PACKAGING INC., FIBERWEB, LLC, LETICA CORPORATION, PLIANT, LLC, PRIME LABEL & SCREEN, INC., PRIME LABEL AND SCREEN INCORPORATED, PROVIDENCIA USA, INC.
Assigned to U.S. BANK NATIONAL ASSOCIATION reassignment U.S. BANK NATIONAL ASSOCIATION CORRECTIVE ASSIGNMENT TO CORRECT THE LISTING OF PATENTS PREVIOUSLY RECORDED AT REEL: 055742 FRAME: 0522. ASSIGNOR(S) HEREBY CONFIRMS THE FIRST LIEN PATENT SECURITY AGREEMENT. Assignors: AVINTIV SPECIALTY MATERIALS INC., BERRY FILM PRODUCTS COMPANY, INC., BERRY GLOBAL FILMS, LLC, BERRY GLOBAL, INC., BPREX HEALTHCARE PACKAGING INC., FIBERWEB, LLC, LETICA CORPORATION, PLIANT, LLC, PRIME LABEL & SCREEN, INC., PRIME LABEL AND SCREEN INCORPORATED, PROVIDENCIA USA, INC.
Assigned to U.S. BANK NATIONAL ASSOCIATION reassignment U.S. BANK NATIONAL ASSOCIATION CORRECTIVE ASSIGNMENT TO CORRECT THE LISTING OF PATENTS PREVIOUSLY RECORDED AT REEL: 058954 FRAME: 0677. ASSIGNOR(S) HEREBY CONFIRMS THE FIRST LIEN PATENT SECURITY AGREEMENT. Assignors: AVINTIV SPECIALTY MATERIALS INC., BERRY FILM PRODUCTS COMPANY, INC., BERRY GLOBAL FILMS, LLC, BERRY GLOBAL, INC., BPREX HEALTHCARE PACKAGING INC., FIBERWEB, LLC, LETICA CORPORATION, PLIANT, LLC, PRIME LABEL & SCREEN, INC., PRIME LABEL AND SCREEN INCORPORATED, PROVIDENCIA USA, INC.
Assigned to U.S. BANK NATIONAL ASSOCIATION reassignment U.S. BANK NATIONAL ASSOCIATION CORRECTIVE ASSIGNMENT TO CORRECT THE LISTING OF PATENTS PREVIOUSLY RECORDED ON REEL 054840 FRAME 0047. ASSIGNOR(S) HEREBY CONFIRMS THE FIRST LIEN PATENT SECURITY AGREEMENT. Assignors: AVINTIV SPECIALTY MATERIALS INC., BERRY FILM PRODUCTS COMPANY, INC., BERRY GLOBAL FILMS, LLC, BERRY GLOBAL, INC., BPREX HEALTHCARE PACKAGING INC., FIBERWEB, LLC, LETICA CORPORATION, PLIANT, LLC, PRIME LABEL & SCREEN, INC., PRIME LABEL AND SCREEN INCORPORATED, PROVIDENCIA USA, INC.
Assigned to U.S. BANK TRUST COMPANY, NATIONAL ASSOCIATION reassignment U.S. BANK TRUST COMPANY, NATIONAL ASSOCIATION SECURITY INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: AVINTIV SPECIALTY MATERIALS INC., BERRY FILM PRODUCTS COMPANY, INC., BERRY GLOBAL FILMS, LLC, BERRY GLOBAL, INC., BPREX HEALTHCARE PACKAGING INC, FIBERWEB, LLC, LETICA CORPORATION, PLIANT, LLC, PROVIDENCIA USA, INC.
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/18Layered products comprising a layer of synthetic resin characterised by the use of special additives
    • B32B27/20Layered products comprising a layer of synthetic resin characterised by the use of special additives using fillers, pigments, thixotroping agents
    • B32B27/205Layered products comprising a layer of synthetic resin characterised by the use of special additives using fillers, pigments, thixotroping agents the fillers creating voids or cavities, e.g. by stretching
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/16Articles comprising two or more components, e.g. co-extruded layers
    • B29C48/18Articles comprising two or more components, e.g. co-extruded layers the components being layers
    • B29C48/21Articles comprising two or more components, e.g. co-extruded layers the components being layers the layers being joined at their surfaces
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/001Combinations of extrusion moulding with other shaping operations
    • B29C48/0018Combinations of extrusion moulding with other shaping operations combined with shaping by orienting, stretching or shrinking, e.g. film blowing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
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    • B29C48/08Flat, e.g. panels flexible, e.g. films
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
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    • B29C48/914Cooling of flat articles, e.g. using specially adapted supporting means cooling drums
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/911Cooling
    • B29C48/9135Cooling of flat articles, e.g. using specially adapted supporting means
    • B29C48/915Cooling of flat articles, e.g. using specially adapted supporting means with means for improving the adhesion to the supporting means
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/911Cooling
    • B29C48/9135Cooling of flat articles, e.g. using specially adapted supporting means
    • B29C48/915Cooling of flat articles, e.g. using specially adapted supporting means with means for improving the adhesion to the supporting means
    • B29C48/916Cooling of flat articles, e.g. using specially adapted supporting means with means for improving the adhesion to the supporting means using vacuum
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/911Cooling
    • B29C48/9135Cooling of flat articles, e.g. using specially adapted supporting means
    • B29C48/915Cooling of flat articles, e.g. using specially adapted supporting means with means for improving the adhesion to the supporting means
    • B29C48/9165Electrostatic pinning
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/911Cooling
    • B29C48/9135Cooling of flat articles, e.g. using specially adapted supporting means
    • B29C48/915Cooling of flat articles, e.g. using specially adapted supporting means with means for improving the adhesion to the supporting means
    • B29C48/917Cooling of flat articles, e.g. using specially adapted supporting means with means for improving the adhesion to the supporting means by applying pressurised gas to the surface of the flat article
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C55/00Shaping by stretching, e.g. drawing through a die; Apparatus therefor
    • B29C55/02Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
    • B29C55/04Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets uniaxial, e.g. oblique
    • B29C55/08Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets uniaxial, e.g. oblique transverse to the direction of feed
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C55/00Shaping by stretching, e.g. drawing through a die; Apparatus therefor
    • B29C55/02Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
    • B29C55/10Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial
    • B29C55/12Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial
    • B29C55/14Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial successively
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C55/00Shaping by stretching, e.g. drawing through a die; Apparatus therefor
    • B29C55/02Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
    • B29C55/10Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial
    • B29C55/12Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial
    • B29C55/14Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial successively
    • B29C55/146Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial successively firstly transversely to the direction of feed and then parallel thereto
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C55/00Shaping by stretching, e.g. drawing through a die; Apparatus therefor
    • B29C55/02Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
    • B29C55/18Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets by squeezing between surfaces, e.g. rollers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C71/00After-treatment of articles without altering their shape; Apparatus therefor
    • B29C71/02Thermal after-treatment
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/06Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B27/08Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/12Layered products comprising a layer of synthetic resin next to a fibrous or filamentary layer
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/28Layered products comprising a layer of synthetic resin comprising synthetic resins not wholly covered by any one of the sub-groups B32B27/30 - B32B27/42
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
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Definitions

  • the present disclosure relates to polymeric materials, and particularly to polymeric films. More particularly, the present disclosure relates to multi-layer polymeric films having a microporous core layer formed from polymeric material and filler.
  • a multi-layer non-breathable film is made using a manufacturing process.
  • the manufacturing process comprises the steps of extruding a composition to form a molten web, casting the molten web to form a quenched film, and stretching the quenched film to form the microporous breathable film.
  • two or more extrudable materials are co-extruded to form the molten web.
  • the quenched film is formed from the molten web by casting the molten web against a surface of a chill roll using a vacuum box and/or blowing air (e.g., an air knife and/or an air blanket).
  • a multi-layer film in accordance with the present disclosure comprises at least one cavitated core layer and at least one non-cavitated skin layer.
  • the at least one cavitated core layer is microporous and breathable.
  • the at least one non-cavitated skin layer is non-microporous and non-breathable.
  • a multi-layer non-breathable film in accordance with the present disclosure comprises first and second non-cavitated skin layers, at least one cavitated core layer disposed between the first and second non-cavitated skin layers, and at least one polar polymer layer disposed between the first and second non-cavitated skin layers.
  • the at least one polar polymer layer comprises a hygroscopic polymer.
  • a partially breathable multi-layer film in accordance with the present disclosure comprises at least one cavitated core layer and at least one skin layer having one or a plurality of discontinuities therein.
  • the multi-layer film includes at least one microporous breathable region and at least one non-microporous non-breathable region.
  • a personal hygiene product comprises at least one inner multi-layer film in accordance with the present disclosure and at least one outer non-woven layer. At least a portion of a non-cavitated skin layer of the inner multi-layer film is bonded to at least a portion of the outer non-woven layer.
  • FIG. 1 is a diagrammatic view of a representative embodiment of a multi-layer film that includes two layers;
  • FIG. 2 is a diagrammatic view of an exemplary process for machine direction (MD) stretching of a polymeric film
  • FIG. 3 is a diagrammatic view of an exemplary process for cross-directional (CD) stretching of a polymeric film
  • FIG. 4 is a diagrammatic view of an exemplary process for intermeshing gears (IMG) stretching of a polymeric film
  • FIG. 5 is a diagrammatic view of an exemplary process for casting a molten web against a chill roll using a vacuum box;
  • FIG. 6 is a diagrammatic view of an exemplary process for casting a molten web against a chill roll using an air knife
  • FIG. 7 is a diagrammatic view of a representative embodiment of a multi-layer non-breathable film that includes three layers;
  • FIG. 8 is a diagrammatic view of a representative embodiment of a multi-layer non-breathable film bonded to a non-woven material
  • FIG. 9 is a diagrammatic view of a representative embodiment of a multi-layer non-breathable film that includes five layers.
  • FIG. 10 is a diagrammatic view of a representative embodiment of a multi-layer partially-breathable film that includes two layers.
  • the multi-layer film 2 includes a cavitated core layer 3 and a non-cavitated skin layer 13 .
  • the cavitated core layer 3 includes a thermoplastic polymer 4 and a solid filler 6 dispersed in the thermoplastic polymer 4 .
  • the cavitated core layer 3 includes a combination of two or more thermoplastic polymers 4 and/or a combination of two or more solid fillers 6 .
  • the non-cavitated skin layer 13 contains a thermoplastic polymer (e.g., which may be the same as or different than the thermoplastic polymer 4 in the cavitated core layer 3 ).
  • the non-cavitated skin layer 13 includes a combination of two or more thermoplastic polymers 4 .
  • the cavitated core layer 3 includes an interconnected network of micropores 8 formed in the thermoplastic polymer resin 4 .
  • the micropores 8 are smaller in size than the size of a typical water droplet but larger in size than a water vapor molecule.
  • the micropores 8 permit the passage of water vapor but minimize or block the passage of liquid water.
  • Two representative pathways for the transmission of water vapor through the cavitated core layer 3 are shown by the dashed lines 10 and 12 in FIG. 1 .
  • a precursor film containing at least one cavitated core layer 3 (e.g., containing a thermoplastic polymer 4 and a solid filler 6 dispersed in the thermoplastic polymer 4 ) and at least one non-cavitated skin layer 13 (e.g., containing a thermoplastic polymer 4 ) may be produced by either a cast film process or a blown film process.
  • the film thus produced may then be stretched by one or more stretching processes.
  • the stretching process moves (e.g., pulls) polymeric material away from the surface of solid filler dispersed therein, thereby forming the micropores 8 .
  • stretching may be achieved via machine direction (MD) orientation by a process analogous to that shown in simplified schematic form in FIG. 2 .
  • the film 14 shown in FIG. 2 may be passed between at least two pairs of rollers in the direction of an arrow 15 .
  • first roller 16 and a first nip 20 run at a slower speed (V 1 ) than the speed (V 2 ) of a second roller 18 and a second nip 22 .
  • V 1 slower speed
  • V 2 speed of a second roller 18 and a second nip 22
  • the ratio of V 2 /V 1 determines the degree to which the film 14 is stretched. Since there may be enough drag on the roll surface to prevent slippage, the process may alternatively be run with the nips open.
  • the first nip 20 and the second nip 22 are optional.
  • stretching may be achieved via transverse or cross-directional (CD) stretching by a process analogous to that shown in simplified schematic form in FIG. 3 .
  • the film 24 shown in FIG. 3 may be moved in the direction of the arrow 28 while being stretched sideways on a tenter frame in the directions of doubled-headed arrow 30 .
  • the tenter frame includes a plurality of attachment mechanisms 26 configured for gripping the film 24 along its side edges.
  • stretching may be achieved via intermeshing gears (IMG) stretching by a process analogous to the one shown in simplified schematic form in FIG. 4 .
  • IMG intermeshing gears
  • a film 32 may be moved between a pair of grooved or toothed rollers as shown in FIG. 4 in the direction of arrow 33 .
  • the first toothed roller 34 may be rotated in a clockwise direction while the second toothed roller 36 may be rotated in a counterclockwise direction.
  • localized stresses may be applied that stretch the film 32 and introduce interconnecting micropores therein analogous to the micropores 8 shown in FIG. 1 .
  • the film 32 may be stretched in the machine direction (MD), the cross direction (CD), at oblique angles to the MD, or in any combination thereof.
  • a precursor film containing at least one cavitated core layer 3 (e.g., containing a thermoplastic polymer 4 and a solid filler 6 dispersed in the thermoplastic polymer 4 ) and at least one non-cavitated skin layer 13 (e.g., containing a thermoplastic polymer 4 ) may be stretched to form a multi-layer film 2 in accordance with the present disclosure.
  • the precursor film may be prepared by mixing together the thermoplastic polymer 4 (or a combination of thermoplastic polymers 4 ), the solid filler 6 (or a combination of solid fillers 6 ), and any optional components until blended, heating the mixture, and then co-extruding the heated mixture with at least one additional extrudable material to form a molten web.
  • the at least one additional extrudable material may contain a thermoplastic polymer 4 (or a combination of thermoplastic polymers 4 ).
  • a suitable film-forming process may be used to form a precursor film en route to forming a multi-layer film.
  • the precursor film may be manufactured by casting or extrusion using blown-film, co-extrusion, or single-layer extrusion techniques and/or the like.
  • the precursor film may be wound onto a winder roll for subsequent stretching in accordance with the present disclosure.
  • the precursor film may be manufactured in-line with a film stretching apparatus such as shown in one or more of FIGS. 2-4 .
  • the precursor film may also contain other optional components to improve the film properties or processing of the film.
  • Representative optional components include but are not limited to anti-oxidants (e.g., added to prevent polymer degradation and/or to reduce the tendency of the film to discolor over time) and processing aids (e.g., added to facilitate extrusion of the precursor film).
  • the amount of one or more anti-oxidants in the precursor film is less than about 1% by weight of the film and the amount of one or more processing aids is less than about 5% by weight of the film.
  • Additional optional additives include but are not limited to whitening agents (e.g., titanium dioxide), which may be added to increase the opacity of the film.
  • the amount of one or more whitening agents is less than about 10% by weight of the film.
  • Further optional components include but are not limited to antiblocking agents (e.g., diatomaceous earth) and slip agents (e.g. erucamide a.k.a. erucylamide), which may be added to allow film rolls to unwind properly and to facilitate secondary processing (e.g., diaper making).
  • the amount of one or more antiblocking agents and/or one or more slip agents is less than about 5% by weight of the film.
  • Further additional optional additives include but are not limited to scents, deodorizers, pigments other than white, noise reducing agents, and/or the like, and combinations thereof.
  • the amount of one or more scents, deodorizers, pigments other than white, and/or noise reducing agents is less than about 10% by weight of the film.
  • the precursor film Prior to stretching, the precursor film may have an initial basis weight of less than about 100 grams per square meter (gsm). In one example, the precursor film has an initial basis weight of less than about 75 gsm.
  • a multi-layer film 2 in accordance with the present disclosure is formed via a blown film process.
  • a multi-layer film 2 in accordance with the present disclosure is formed via a cast film process.
  • the cast film process involves the extrusion of molten polymers through an extrusion die to form a thin film.
  • the film is pinned to the surface of a chill roll with an air knife, an air blanket, and/or a vacuum box.
  • a process for making a multi-layer film 2 in accordance with the present disclosure includes (a) extruding two or more extrudable materials to form a molten web, wherein at least one of the two or more extrudable materials comprises a first polyolefin and an inorganic filler, and at least another of the two or more extrudable materials comprises a second polyolefin, (b) casting the molten web against a surface of a chill roll using an air knife, an air blanket, a vacuum box, or a combination thereof to form a quenched film, and (c) stretching the quenched film to form the multi-layer film 2 .
  • the first olefin and the second olefin may be the same or different.
  • a cavitated core layer 3 exhibiting surprisingly and unexpectedly improved properties as compared to other microporous breathable films may be prepared.
  • these properties may include reduced basis weight, increased strain at peak machine direction, increased tensile strength at peak machine direction, increased tensile strength at 5% strain machine direction, increased secant modulus machine direction (1%), increased Dart Impact Strength, and/or the like, and combinations thereof.
  • the molten web is cast against the surface of the chill roll under negative pressure using a vacuum box as shown in simplified schematic form in FIG. 5 .
  • a vacuum box works by evacuating air between the film and the surface of the chill roll.
  • a film 46 is extruded from an extrusion die 40 in the direction of arrow 47 and quenched from the molten state with a vacuum box 42 .
  • the vacuum box 42 draws a vacuum behind the molten web 46 in the direction of arrow 44 to draw the film 46 down onto the chill roll 38 .
  • the vacuum drawn in the direction of arrow 44 removes the entrained air between the surface of the chill roll 38 and the film 46 .
  • the vacuum box process is not subject to draw resonance for high molecular weight polymers that would tend to extrude unstable thickness in a nipped quench process due to the draw resonance phenomenon.
  • the molten polymer may exit the die 40 and hit the chill roll 38 within a smaller distance than in an embossed process.
  • the melt curtain is configured to hit the chill roll 38 within a distance of less than about 12 inches, 11 inches, 10 inches, 9 inches, 8 inches, 7 inches, 6 inches, 5 inches, 4 inches, 3, inches, 2 inches, or 1 inch.
  • the melt curtain is configured to exit the die and hit the roll within a distance of less than about 3 inches and, in some examples, within a distance of about or less than 1 inch.
  • One advantage of reducing the distance between the die 40 and the roll surface 38 as compared to in a nipped quench process is that smaller distances are less susceptible to the phenomenon of neck-in.
  • Neck-in refers to a reduction in width of the molten web that occurs as the web leaves the die.
  • the molten web is cast against the surface of the chill roll under positive pressure using an air knife or air blanket, as shown in simplified schematic form in FIG. 6 .
  • An air knife works to promote web quenching by gently blowing a high-velocity, low-volume air curtain over the molten film, thereby pinning the molten film to the chill roll for solidification.
  • a film 54 is extruded from an extrusion die 50 in the direction of arrow 55 and quenched from the molten state with an air knife 52 blowing an air curtain over the molten film 54 , thereby pinning the molten web 54 against a surface of the chill roll 48 .
  • An air blanket also called a soft box
  • the air curtain is low velocity and high volume.
  • the molten web is cast against the surface of the chill roll under a combination of negative pressure from a vacuum box, as shown in FIG. 5 , and positive pressure from an air knife, as shown in FIG. 6 .
  • an exit temperature of cooling fluid passing through the chill roll is between about 50 degrees Fahrenheit and about 130 degrees Fahrenheit and, in some examples, between about 75 degrees Fahrenheit and about 130 degrees Fahrenheit.
  • thermoplastic polymer 4 (or combination of thermoplastic polymers 4 ) used to make a non-cavitated skin layer 13 and/or a cavitated core layer 3 of a multi-layer film 2 in accordance with the present disclosure is not restricted, and may include all manner of thermoplastic polymers.
  • the thermoplastic polymer is a polyolefin, including but not limited to homopolymers, copolymers, terpolymers, and/or blends thereof.
  • LDPE low density polyethylene
  • HDPE high density polyethylene
  • LLDPE linear low density polyethylene
  • ULDPE ultra-low density polyethylene
  • polypropylene ethylene-propylene copolymers
  • polymers made using a single-site catalyst ethylene maleic anhydride copolymers (EMAs), ethylene vinyl acetate copolymers (EVAs), polymers made using Zeigler-Natta catalysts, styrene-containing block copolymers, and/or the like, and combinations thereof.
  • EMAs ethylene maleic anhydride copolymers
  • EVAs ethylene vinyl acetate copolymers
  • Zeigler-Natta catalysts Zeigler-Natta catalysts
  • styrene-containing block copolymers and/or the like, and combinations thereof.
  • ULDPE may be produced by a variety of processes, including but not limited to gas phase, solution and slurry polymerization as described in The Wiley Encyclopedia of Packaging Technology , pp. 748-50 (Aaron L. Brody et al. eds., 2nd Ed. 1997), incorporated by reference above, except that in the event of any inconsistent disclosure or definition from the present specification, the disclosure or definition herein shall be deemed to prevail.
  • ULDPE may be manufactured using a Ziegler-Natta catalyst, although a number of other catalysts may also be used.
  • ULDPE may be manufactured with a metallocene catalyst.
  • ULDPE may be manufactured with a catalyst that is a hybrid of a metallocene catalyst and a Ziegler-Natta catalyst.
  • Methods for manufacturing ULDPE are also described in U.S. Pat. Nos. 5,399,426, 4,668,752, 3,058,963, 2,905,645, 2,862,917, and 2,699,457, each of which is incorporated by reference herein in its entirety, except that in the event of any inconsistent disclosure or definition from the present specification, the disclosure or definition herein shall be deemed to prevail.
  • the density of ULDPE is achieved by copolymerizing ethylene with a sufficient amount of one or more monomers.
  • the monomers are selected from 1-butene, 1-hexene, 4-methyl-1-pentene, 1-octene, and combinations thereof.
  • Methods for manufacturing polypropylene are described in Kirk - Othmer Concise Encyclopedia of Chemical Technology , pp. 1420-1421 (Jacqueline I. Kroschwitz et al. eds., 4th Ed. 1999), which is incorporated herein by reference, except that in the event of any inconsistent disclosure or definition from the present specification, the disclosure or definition herein shall be deemed to prevail.
  • a polyolefin for use in accordance with the present disclosure includes polyethylene, polypropylene, or a combination thereof.
  • the polyethylene includes linear low density polyethylene which, in some embodiments, includes a metallocene polyethylene.
  • the polyethylene includes a combination of linear low density polyethylene and low density polyethylene.
  • the polyolefin consists essentially of only linear low density polyethylene.
  • an extrudable material to be extruded in accordance with the present disclosure may further include a solid filler.
  • the solid filler is not restricted, and may include all manner of inorganic or organic materials that are (a) non-reactive with thermoplastic polymer, (b) configured for being uniformly blended and dispersed in the thermoplastic polymer, and (c) configured to promote a microporous structure within the film when the film is stretched.
  • the solid filler includes an inorganic filler.
  • Representative inorganic fillers for use in accordance with the present disclosure include but are not limited to sodium carbonate, calcium carbonate, magnesium carbonate, barium sulfate, magnesium sulfate, aluminum sulfate, magnesium oxide, calcium oxide, alumina, mica, talc, silica, clay (e.g., non-swellable clay), glass spheres, titanium dioxide, aluminum hydroxide, zeolites, and a combination thereof.
  • the inorganic filler includes an alkali metal carbonate, an alkaline earth metal carbonate, an alkali metal sulfate, an alkaline earth metal sulfate, or a combination thereof.
  • the inorganic filler includes calcium carbonate.
  • the solid filler includes a polymer (e.g., high molecular weight high density polyethylene, polystyrene, nylon, blends thereof, and/or the like).
  • a polymer e.g., high molecular weight high density polyethylene, polystyrene, nylon, blends thereof, and/or the like.
  • the use of polymer fillers creates domains within the thermoplastic polymer matrix. These domains are small areas, which may be spherical, where only the polymer filler is present as compared to the remainder of the thermoplastic matrix where no polymer filler is present. As such, these domains act as particles.
  • the solid filler 6 provided in a composition to be extruded in accordance with the present disclosure may be used to produce micropores 8 of multi-layer film 2 , as shown in FIG. 1 .
  • the dimensions of the solid filler 6 particles may be varied based on a desired end use (e.g., the desired properties of cavitated core layer 3 ).
  • the average particle size of a solid filler particle ranges from about 0.1 microns to about 15 microns. In illustrative embodiments, the average particle size ranges from about 1 micron to about 5 microns and, in some examples, from about 1 micron to about 3 microns.
  • the average particle size may be one of several different values or fall within one of several different ranges.
  • an average particle size of the solid filler to be one of the following values: about 0.1 microns, 0.2 microns, 0.3 microns, 0.4 microns, 0.5 microns, 0.6 microns, 0.7 microns, 0.8 microns, 0.9 microns, 1.0 microns, 1.1 microns, 1.2 microns, 1.3 microns, 1.4 microns, 1.5 microns, 1.6 microns, 1.7 microns, 1.8 microns, 1.9 microns, 2.0 microns, 2.1 microns, 2.2 microns, 2.3 microns, 2.4 microns, 2.5 microns, 2.6 microns, 2.7 microns, 2.8 microns, 2.9 microns, 3.0 microns, 3.5 microns, 4.0 microns, 4.5 microns, 5.0 microns, 5.5 microns, 6.0 microns, 6.5 microns, 7.0 micron
  • the average particle size of the solid filler 6 provided in a composition to be extruded in accordance with the present disclosure is in one of the following ranges: about 0.1 microns to 15 microns, 0.1 microns to 14 microns, 0.1 microns to 13 microns, 0.1 microns to 12 microns, 0.1 microns to 11 microns, 0.1 microns to 10 microns, 0.1 microns to 9 microns, 0.1 microns to 8 microns, 0.1 microns to 7 microns, 0.1 microns to 6 microns, 0.1 microns to 5 microns, 0.1 microns to 4 microns, and 0.1 microns to 3 microns.
  • the average particle size of the solid filler 6 is in one of the following ranges: about 0.1 microns to 5 microns, 0.2 microns to 5 microns, 0.3 microns to 5 microns, 0.4 microns to 5 microns, 0.5 microns to 5 microns, 0.6 microns to 5 microns, 0.7 microns to 5 microns, 0.8 microns to 5 microns, 0.9 microns to 5 microns, and 1.0 microns to 5 microns.
  • the average particle size of the solid filler 6 is in one of the following ranges: about 0.1 microns to 4.9 microns, 0.2 microns to 4.8 microns, 0.3 microns to 4.7 microns, 0.4 microns to 4.6 microns, 0.5 microns to 4.5 microns, 0.6 microns to 4.4 microns, 0.7 microns to 4.3 microns, 0.8 microns to 4.2 microns, 0.9 microns to 4.1 microns, and 1.0 microns to 4.0 microns.
  • the amount of solid filler used in accordance with the present disclosure includes from about 30% by weight to about 75% by weight of the material to be extruded, quenched film formed from the extrusion of two or more extrudable materials, and/or multi-layer film formed from the quenched film. In further illustrative embodiments, the amount of solid filler used in accordance with the present disclosure includes from about 50% by weight to about 75% by weight of the material to be extruded, quenched film formed from the extrusion of two or more extrudable materials, and/or multi-layer film formed from the quenched film.
  • filler may also be employed, an amount of solid filler that is less than about 30% by weight may not be sufficient to impart uniform breathability to a film. Conversely, amounts of filler greater than about 75% by weight may be difficult to blend with the polymer and may cause a loss in strength in the final film.
  • the amount of solid filler 6 may be varied based on a desired end use (e.g., the desired properties of the cavitated core layer 3 ). In one example, the amount of solid filler 6 ranges from about 40% to about 60% by weight of the material to be extruded, quenched film formed from the extrusion of the two or more extrudable materials, and/or multi-layer film formed from the quenched film. In another example, the amount of solid filler 6 ranges from about 45% to about 55% by weight of the material to be extruded, quenched film formed from the extrusion of the two or more extrudable materials, and/or multi-layer film formed from the quenched film.
  • the amount of solid filler 6 may be one of several different values or fall within one of several different ranges. For example, it is within the scope of the present disclosure to select an amount of the solid filler 6 to be one of the following values: about 30%, 31%, 32%, 33%, 34%, 35%, 36%, 37%, 38%, 39%, 40%, 41%, 42%, 43%, 44%, 45%, 46%, 47%, 48%, 49%, 50%, 51%, 52%, 53%, 54%, 55%, 56%, 57%, 58%, 59%, 60%, 61%, 62%, 63%, 64%, 65%, 66%, 67%, 68%, 69%, 70%, 71%, 72%, 73%, 74%, or 75% by weight of the material to be extruded, quenched film formed from the extrusion of the two or more extrudable materials, and/or multi-layer film formed from the quenched film.
  • the amount of the solid filler 6 is in one of the following ranges: about 31% to 75%, 32% to 75%, 33% to 75%, 34% to 75%, 35% to 75%, 36% to 75%, 37% to 75%, 38% to 75%, 39% to 75%, 40% to 75%, 41% to 75%, 42% to 75%, 43% to 75%, 44% to 75%, and 45% to 75% by weight of the material to be extruded, quenched film formed from the extrusion of the two or more extrudable materials, and/or multi-layer film formed from the quenched film.
  • the amount of the solid filler is in one of the following ranges: about 30% to 74%, 30% to 73%, 30% to 72%, 30% to 71%, 30% to 70%, 30% to 69%, 30% to 68%, 30% to 67%, 30% to 66%, 30% to 65%, 30% to 64%, 30% to 63%, 30% to 62%, 30% to 61%, 30% to 60%, 30% to 59%, 30% to 58%, 30% to 57%, 30% to 56%, 30% to 55%, 30% to 54%, 30% to 53%, 30% to 52%, 30% to 51%, 30% to 50%, 30% to 49%, 30% to 48%, 30% to 47%, 30% to 46%, and 30% to 45% by weight of the material to be extruded, quenched film formed from the extrusion of the two or more extrudable materials, and/or multi-layer film formed from the quenched film.
  • the amount of the solid filler is in one of the following ranges: about 31% to 74%, 32% to 73%, 33% to 72%, 34% to 71%, 35% to 70%, 36% to 69%, 37% to 68%, 38% to 67%, 39% to 66%, 40% to 65%, 41% to 64%, 42% to 63%, 43% to 62%, 44% to 61%, 45% to 60%, 45% to 59%, 45% to 58%, 45% to 57%, 45% to 56%, and 45% to 55% by weight of the material to be extruded, quenched film formed from the extrusion of the two or more extrudable materials, and/or multi-layer film formed from the quenched film.
  • filler loading may be conveniently expressed in terms of weight percentages
  • the phenomenon of microporosity may alternatively be described in terms of volume percent of filler relative to total volume.
  • 35% by weight CaCO 3 corresponds to a filler loading of about 15% by volume ⁇ (0.35/2.7)/(0.65/0.9+0.35/2.7) ⁇ .
  • the 75 weight percent upper end of the range described above corresponds to about 56% by volume of CaCO 3 .
  • the amount of filler may be adjusted to provide comparable volume percentages for alternative solid fillers that have different (e.g., unusually low or high) specific gravities as compared to calcium carbonate.
  • the filler particles may be coated with a fatty acid and/or other suitable processing acid.
  • Representative fatty acids for use in this context include but are not limited to stearic acid or longer chain fatty acids.
  • the type of stretching used to transform a quenched film into a multi-layer film 2 in accordance with the present disclosure is not restricted. All manner of stretching processes and combinations of stretching processes that are capable of moving (e.g., pulling) polymeric material 4 away from the surface of solid filler 6 dispersed therein in order to form micropores 8 in a cavitated core layer 3 are contemplated for use.
  • the stretching includes cross-directional stretching.
  • the stretching includes CD-IMG stretching.
  • the stretching includes MD stretching.
  • the stretching includes MD IMG stretching.
  • the stretching includes cold draw.
  • the stretching includes a combination of two or more different types of stretching including but not limited to MD stretching, CD IMG stretching, MD IMG stretching, cold draw, and/or the like.
  • the stretching includes a combination of CD IMG stretching and cold draw (which, in some embodiments, is performed subsequently to the CD IMG stretching).
  • the stretching includes CD-IMG stretching followed by downweb MD stretching.
  • the type of stretching used to transform a quenched film into a multi-layer film 2 in accordance with the present disclosure includes CD IMG stretching.
  • at least a portion of the stretching is performed at a temperature above ambient temperature. In one example, at least a portion of the stretching is performed at a temperature of between about 60 degrees Fahrenheit and about 200 degrees Fahrenheit.
  • a process for making a multi-layer film 2 in accordance with the present disclosure further includes annealing the multi-layer film 2 .
  • the annealing is performed at a temperature of between about 75 degrees Fahrenheit and about 225 degrees Fahrenheit.
  • a multi-layer film 2 prepared in accordance with the present disclosure may have reduced basis weight, increased tensile strength at peak machine direction, increased tensile strength at 5% strain machine direction, increased secant modulus machine direction (1%), and/or increased Dart Impact Strength as compared to conventional multi-layer films containing a microporous breathable layer.
  • the basis weight of a multi-layer film 2 in accordance with the present disclosure may be varied based on a desired end use (e.g., the desired properties and/or applications of the multi-layer film 2 ). In one example, the basis weight ranges from about 5 gsm to about 30 gsm. In another example, the basis weight ranges from about 6 gsm to about 25 gsm. In illustrative embodiments, the basis weight is less than about 14 gsm and, in some examples, less than about 12 gsm.
  • basis weights outside this range may also be employed (e.g., basis weights above about 30 gsm), lower basis weights minimize material cost as well as maximize consumer satisfaction (e.g., a thinner film may provide increased comfort to the user of a personal hygiene product that includes the film).
  • the basis weight of a multi-layer film 2 in accordance with the present disclosure may be one of several different values or fall within one of several different ranges.
  • a basis weight to be one of the following values: about 30 gsm, 29 gsm, 28 gsm, 27 gsm, 26 gsm, 25 gsm, 24 gsm, 23 gsm, 22 gsm, 21 gsm, 20 gsm, 19 gsm, 18 gsm, 17 gsm, 16 gsm, 15 gsm, 14 gsm, 13 gsm, 12 gsm, 11 gsm, 10 gsm, 9 gsm, 8 gsm, 7 gsm, 6 gsm, or 5 gsm.
  • the basis weight of the multi-layer film 2 is in one of the following ranges: about 5 gsm to 30 gsm, 6 gsm to 30 gsm, 7 gsm to 30 gsm, 8 gsm to 30 gsm, 9 gsm to 30 gsm, 10 gsm to 30 gsm, 11 gsm to 30 gsm, 12 gsm to 30 gsm, 13 gsm to 30 gsm, and 14 gsm to 30 gsm.
  • the basis weight of the microporous breathable film is in one of the following ranges: about 5 gsm to 29 gsm, 5 gsm to 28 gsm, 5 gsm to 27 gsm, 5 gsm to 26 gsm, 5 gsm to 25 gsm, 5 gsm to 24 gsm, 5 gsm to 23 gsm, 5 gsm to 22 gsm, 5 gsm to 21 gsm, 5 gsm to 20 gsm, 5 gsm to 19 gsm, 5 gsm to 18 gsm, 5 gsm to 17 gsm, 5 gsm to 16 gsm, 5 gsm to 15 gsm, 5 gsm to 14 gsm, 5 gsm to 13 gsm, 5 gsm to 12 gsm, 5 gsm to 11
  • the basis weight of the multi-layer film 2 is in one of the following ranges: about 6 gsm to 29 gsm, 7 gsm to 29 gsm, 7 gsm to 28 gsm, 7 gsm to 27 gsm, 7 gsm to 26 gsm, 7 gsm to 25 gsm, 7 gsm to 24 gsm, 7 gsm to 23 gsm, 7 gsm to 22 gsm, 7 gsm to 21 gsm, 7 gsm to 20 gsm, 7 gsm to 19 gsm, 7 gsm to 18 gsm, 7 gsm to 17 gsm, 7 gsm to 16 gsm, 7 gsm to 15 gsm, 7 gsm to 14 gsm, 7 gsm to 13 gsm, 7 gsm to 12 gs
  • a multi-layer film 2 in accordance with the present disclosure exhibits greater tensile strength at peak machine direction than conventional multi-layer films of similar basis weight.
  • the basis weight of a multi-layer film 2 in accordance with the present disclosure may be varied based on a desired tensile strength at peak machine direction.
  • a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a tensile strength at peak machine direction of at least about 500 grams/inch (g/in).
  • a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a tensile strength at peak machine direction of at least about 600 grams/inch. In a further example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a tensile strength at peak machine direction of at least about 700 g/in. In a further example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a tensile strength at peak machine direction of at least about 800 g/in.
  • the tensile strength at peak machine direction of a multi-layer film 2 in accordance with the present disclosure may be one of several different values or fall within one of several different ranges.
  • the tensile strength at peak machine direction of the multi-layer film 2 is in one of many different ranges.
  • a multi-layer film 2 in accordance with the present disclosure exhibits greater increased tensile strength at 5% strain machine direction than conventional multi-layer films of similar basis weight.
  • the basis weight of a multi-layer film 2 in accordance with the present disclosure may be varied based on a desired tensile strength at 5% strain machine direction.
  • a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a tensile strength at 5% strain machine direction of at least about 170 grams/inch (g/in).
  • a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a tensile strength at 5% strain machine direction of at least about 180 grams/inch. In a further example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a tensile strength at 5% strain machine direction of at least about 190 g/in. In a further example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a tensile strength at 5% strain machine direction of at least about 200 g/in.
  • the tensile strength at 5% strain machine direction of a multi-layer film 2 in accordance with the present disclosure may be one of several different values or fall within one of several different ranges.
  • the tensile strength at 5% strain machine direction of the multi-layer film 2 is in one of many different ranges.
  • a multi-layer film 2 in accordance with the present disclosure exhibits greater increased secant modulus machine direction (1%) than conventional multi-layer films of similar basis weight.
  • the basis weight of a multi-layer film 2 in accordance with the present disclosure may be varied based on a desired secant modulus machine direction (1%).
  • a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a secant modulus machine direction (1%) of at least about 20,000 pounds/inch (psi).
  • a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a secant modulus machine direction (1%) of at least about 25,000 psi. In a further example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a secant modulus machine direction (1%) of at least about 30,000 psi. In a further example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a secant modulus machine direction (1%) of at least about 35,000 psi.
  • the secant modulus machine direction (1%) of a multi-layer film 2 in accordance with the present disclosure may be one of several different values or fall within one of several different ranges.
  • the secant modulus machine direction (1%) of the multi-layer film 2 is in one of many different ranges.
  • a multi-layer film 2 in accordance with the present disclosure exhibits a greater Dart Impact Strength than conventional microporous breathable films of similar basis weight.
  • the basis weight of a multi-layer film 2 in accordance with the present disclosure may be varied based on a desired Dart Impact Strength.
  • a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a Dart Impact Strength of at least about 35 grams.
  • a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a Dart Impact Strength of at least about 40 grams.
  • a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a Dart Impact Strength of at least about 45 grams. In a still further example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a Dart Impact Strength of at least about 50 grams.
  • the Dart Impact Strength of a multi-layer film 2 in accordance with the present disclosure may be one of several different values or fall within one of several different ranges.
  • the Dart Impact Strength of the multi-layer film 2 is also within the scope of the present disclosure for the Dart Impact Strength of the multi-layer film 2 to fall within one of many different ranges.
  • a multi-layer film in accordance with the present disclosure may be manufactured by feed block coextrusion.
  • a multi-layer film in accordance with the present disclosure may be made by blown film (tubular) coextrusion.
  • Methods for feed block and blown film extrusion are described in The Wiley Encyclopedia of Packaging Technology , pp. 233-238 (Aaron L. Brody et al. eds., 2nd Ed. 1997), which is incorporated herein by reference, except that in the event of any inconsistent disclosure or definition from the present specification, the disclosure or definition herein shall be deemed to prevail.
  • Methods for film extrusion are also described in U.S. Pat. No. 6,265,055, the entire contents of which are likewise incorporated by reference herein, except that in the event of any inconsistent disclosure or definition from the present specification, the disclosure or definition herein shall be deemed to prevail.
  • the present disclosure provides a multi-layer film 2 having a single non-cavitated skin layer 13 .
  • the present disclosure also provides a multi-layer non-breathable film 56 having more than one non-cavitated skin layer.
  • the multi-layer non-breathable film 56 shown in FIG. 7 includes a first non-cavitated skin layer 58 , a second non-cavitated skin layer 60 , and at least one cavitated core layer 62 disposed between the first non-cavitated skin layer 58 and the second non-cavitated skin layer 60 .
  • the core layer 62 in FIG. 7 is analogous to the core layer 3 shown in FIG.
  • first non-cavitated skin layer 58 and the second non-cavitated skin layer 60 may have either the same composition as the core layer 62 or a different composition than the core layer 62 .
  • first non-cavitated skin layer 58 and the second non-cavitated skin layer 60 are analogous to the non-cavitated skin layer 13 shown in FIG. 1 and may include a thermoplastic polymer (or combination of thermoplastic polymers).
  • a multi-layer film containing a a first non-cavitated skin layer 59 , a second non-cavitated skin layer 61 , and at least one cavitated core layer 63 disposed between the first non-cavitated skin layer 59 and the second non-cavitated skin layer 61 may be bonded to a non-woven layer 66 to form a multi-layer structure 64 that may, in some embodiments, be used as a backsheet for a diaper, incontinence brief, and/or the like, as further described below.
  • a multi-layer structure 64 may, in some embodiments, be used as a backsheet for a diaper, incontinence brief, and/or the like, as further described below.
  • the non-woven layer 66 may be bonded to one or the other of the first non-cavitated skin layer 59 and the second non-cavitated skin layer 61 .
  • the non-woven layer 66 and the non-cavitated skin layer to which it is adjacent include the same polyolefin.
  • the non-woven layer 66 , the second non-cavitated skin layer 61 , and/or the first non-cavitated skin layer 59 include polypropylene.
  • the non-woven layer 66 , the second non-cavitated skin layer 61 , and/or the first non-cavitated skin layer 59 include polypropylene, and the non-woven layer 66 is bonded to the second non-cavitated skin layer 61 by an ultrasonic weld, as further described below.
  • a multi-layer non-breathable film 68 in accordance with the present disclosure contains a first non-cavitated skin layer 70 , a second non-cavitated skin layer 74 , a first cavitated core layer 72 disposed between the first non-cavitated skin layer 70 and the second non-cavitated skin layer 74 , a second cavitated core layer 76 disposed between the first non-cavitated skin layer 70 and the second non-cavitated skin layer 74 , and at least one polar polymer layer 78 disposed between the first non-cavitated skin layer 70 and the second non-cavitated skin layer 74 .
  • the polar polymer layer 78 is configured to act as an odor barrier that is substantially impermeable to odorants that are nonpolar.
  • the first cavitated core layer 72 and the second cavitated core layer 76 in FIG. 9 are analogous to the cavitated core layer 3 shown in FIG. 1 , and may be prepared by a process analogous to one described above.
  • the first cavitated core layer 72 may be the same as or different than the second cavitated core layer 76 .
  • the first cavitated core layer 72 and the second cavitated core layer 76 may differ from each other in thickness, breathability, pore size, thermoplastic composition, and/or the like.
  • the first cavitated core layer 72 and the second cavitated core layer 76 are the same, and each includes a polyolefin and an inorganic filler dispersed in the polyolefin.
  • the first non-cavitated skin layer 70 and the second non-cavitated skin layer 74 in FIG. 9 are analogous to the non-cavitated skin layer 13 shown in FIG. 1 .
  • the first non-cavitated skin layer 70 may be the same as or different than the second non-cavitated skin layer 74 (e.g., in thickness, plastic composition, and/or the like).
  • the first non-cavitated skin layer 70 and the second non-cavitated skin layer 74 are the same, and each includes a polyolefin.
  • the multi-layer film 68 has a symmetrical structure, and the at least one polar polymer layer 78 is disposed between the first non-cavitated skin layer 70 and the first cavitated core layer 72 on one side, and between the second cavitated core layer 76 and the second non-cavitated skin layer 74 on its other side.
  • the at least one polar polymer layer 78 is disposed between the first non-cavitated skin layer 70 and the first cavitated core layer 72 on one side, and between the second cavitated core layer 76 and the second non-cavitated skin layer 74 on its other side.
  • alternative configurations may likewise be implemented.
  • the polar polymer layer 78 shown in FIG. 9 provides an internal barrier layer and—unlike first cavitated core layer 72 and second cavitated core layer 76 —may be unfilled or substantially unfilled (e.g., contain an amount of solid filler that does not result in the creation of micropores as a result of stretching).
  • the polar polymer layer 78 is comprised of Nylon, polyester, ethylene vinyl alcohol (EVOH) or copolymers of these materials.
  • the polar polymer layer 78 provides an odor barrier.
  • a tie layer (not shown) may be used to combine dissimilar layers (e.g., polar polymer layer 78 and one or both of first cavitated core layer 72 and second cavitated core layer 76 ).
  • an adhesive may be blended in one or more of the adjacent dissimilar layers, thus avoiding delamination of the adjacent, chemically different layers.
  • the internal polar polymer layer 78 is selected from the group consisting of elastomers, polyesters, polyamides, polyetherester copolymers, polyetheramide copolymers, polyurethanes, polyurethane copolymers, poly(etherimide) ester copolymers, polyvinyl alcohols, ionomers, celluloses, nitrocelluloses, and/or the like, and combinations thereof.
  • the at least one polar polymer layer 78 further includes an adhesive which, in some embodiments, includes polyethylene/acrylate copolymer, ethylene/methyl acrylate copolymer, acid-modified acrylate, anhydride-modified acrylate, ethylene vinyl acetate, acid/acrylate-modified ethylene vinyl acetate, anhydride-modified ethylene vinyl acetate, and/or the like, or a combination thereof.
  • the internal polar polymer layer 78 may constitute from about 0.5% to about 30% of the total thickness of the film 68 .
  • the polar polymer layer 78 may constitute from about 1% to about 20% of the total thickness of the film 68 .
  • the polar polymer layer 78 may constitute from about 2% to about 10% of the total thickness of the film 68 .
  • the multi-layer film 68 includes a plurality of polar polymer layers 78 , and the above-described exemplary ranges of thickness percentages may be applied to the sum of the multiple polar polymer layers within the film.
  • Multi-layer non-breathable films 68 in accordance with the present disclosure may include one or more internal polar polymer layers 78 , which may be contiguous with each other or with interposed microporous breathable layers such as first cavitated core layer 72 and second cavitated core layer 76 .
  • one or more polar polymer layers 78 provided in a multi-layer breathable barrier film 68 in accordance with the present disclosure are monolithic and do not contain any fillers that provide sites for the development of micropores.
  • polar polymer layers may contain other additives to confer desired properties to the polar polymer layer.
  • Representative materials for the polar polymer layer 78 include but are not limited to hygroscopic polymers such as ⁇ -caprolactone (available from Solvay Caprolactones), polyether block amides (available from Arkema PEBAX), polyester elastomer (such as Dupont Hytrel or DSM Arnitel) and other polyesters, polyamides, celluloses (e.g., cellulose fibers), nitrocelluloses (e.g., nitrocellulose fibers), ionomers (e.g., ethylene ionomers), and/or the like, and combinations thereof.
  • hygroscopic polymers such as ⁇ -caprolactone (available from Solvay Caprolactones), polyether block amides (available from Arkema PEBAX), polyester elastomer (such as Dupont Hytrel or DSM Arnitel) and other polyesters, polyamides, celluloses (e.g., cellulose fibers), nitrocelluloses (e.g
  • fatty acid salt-modified ionomers as described in the article entitled “Development of New Ionomers with Novel Gas Permeation Properties” ( Journal of Plastic Film and Sheeting, 2007, 23, No. 2, 119-132) may be used as a polar polymer layer 78 .
  • sodium, magnesium, and/or potassium fatty acid salt-modified ionomers may be used to provide desirable water vapor transmission properties.
  • the polar polymer layer 78 is selected from the group consisting of hygroscopic elastomers, polyesters, polyamides, polyetherester copolymers (e.g., a block polyetherester copolymer), polyetheramide copolymers (e.g., a block polyetheramide copolymer), polyurethanes, polyurethane copolymers, poly(etherimide) ester copolymers, polyvinyl alcohols, ionomers, celluloses, nitrocelluloses, and/or the like, and combinations thereof.
  • copolyether ester block copolymers are segmented elastomers having soft polyether segments and hard polyester segments, as described in U.S.
  • copolyether ester block copolymers are sold by DuPont under the trade name HYTREL®.
  • Representative copolyether amide polymers are copolyamides sold under the trade name PEBAX® by Atochem Inc. of Glen Rock, N.J.
  • Representative polyurethanes are thermoplastic urethanes sold under the trade name ESTANE® by the B. F. Goodrich Company of Cleveland, Ohio.
  • Representative copoly(etherimide) esters are described in U.S. Pat. No. 4,868,062.
  • the polar polymer layer 78 may include or be blended with a thermoplastic resin.
  • thermoplastic resins that may be used for this purpose include but are not limited to polyolefins, polyesters, polyetheresters, polyamides, polyether amides, urethanes, and/or the like, and combinations thereof.
  • the thermoplastic polymer may include (a) a polyolefin, such as polyethylene, polypropylene, poly(i-butene), poly(2-butene), poly(i-pentene), poly(2-pentene), poly(3-methyl-1-pentene), poly(4-methyl-1-pentene), 1,2-poly-1,3-butadiene, 1,4-poly-1,3-butadiene, polyisoprene, polychloroprene, polyacrylonitrile, polyvinyl acetate, poly(vinylidene chloride), polystyrene, and/or the like, and combinations thereof; (b) a polyester such as poly(ethylene terephthalate), poly(butylenes)terephthalate, poly(tetramethylene terephthalate), poly(cyclohexylene-1,4-dimethylene terephthalate), poly(oxymethylene-1,4-cyclohexylenemethyleneoxyterephthaloyl
  • the hygroscopic polymer is a hygroscopic elastomer.
  • a variety of additives may be added to the polar polymer layer 78 to provide additional properties such as antimicrobial effects, odor control, static decay, and/or the like.
  • One or more of the polar polymer layer 78 , the first cavitated core layer 72 , and the second cavitated core layer 76 in the multi-layer non-breathable film 68 may include one or more adhesives for adhering the internal polar polymer layer 78 to contiguous layers to form at least a portion of the multi-layer film 68 .
  • adhesive may be components suitable for adhering two or more layers together.
  • adhesives are compatibilizing adhesives that increase the compatibility of the layers as well as adhering the layers to one another. The adhesives may be included in the resin or other extrudable material before extruding that resin into the polar polymer layer 78 .
  • compatibilizing adhesives include but are not limited to polyethylene/acrylate copolymer, ethylene/methyl acrylate copolymer, acid-modified acrylate, anhydride-modified acrylate, ethylene vinyl acetate, acid/acrylate-modified ethylene vinyl acetate, anhydride-modified ethylene vinyl acetate, and/or the like, and combinations thereof.
  • the adhesive when one of the first cavitated core layer 72 , the second cavitated core layer 76 , and the polar polymer layer 78 includes an adhesive, the adhesive may have a relatively high methacrylate content (e.g., a methacrylate content of at least about 20% to 25%).
  • the internal polar polymer layer 78 may be prepared from blends including up to about 50% by weight adhesive and at least about 50% by weight hygroscopic polymer.
  • the hygroscopic polymer may be dried before it is extruded. Feeding pre-dried hygroscopic elastomer in small amounts to an extruder has proven to be effective in avoiding moisture absorption, preventing hydrolysis of the hygroscopic elastomer, and reducing or eliminating the formation of dark blue gels and holes in web. In some higher stretch ratio cases, gels rendered holes and even web break.
  • a multi-layer non-breathable barrier film 68 in accordance with the present disclosure may contain one or a plurality of polar polymer layers 78 , each of which may be placed in any order in the inner layers of the film structure.
  • the polar polymer layer 78 is not placed on the outer surface of the resultant film 68 in order to avoid damage caused by foreign materials.
  • individual polar polymer layers 78 are not placed adjacent to each other inside the film in order to increase efficacy.
  • the individual polar polymer layers 78 may differ from each other in thickness and/or type of thermoplastic polymer.
  • a representative structure for a multi-layer breathable barrier film 68 contains five layers with one polar polymer layer 78 being in the center of the structure and two microporous, breathable cavitated core layers ( 72 and 74 , respectively) being arranged symmetrically around the central polar polymer layer 78 .
  • the five-layer breathable barrier film has a A 1 -C 1 -B-C 2 -A 2 structure as shown in FIG.
  • a 1 represents a first non-cavitated skin layer
  • C 1 represents a first microporous, breathable cavitated core layer
  • B represents a polar polymer layer
  • C 2 represents a second microporous breathable cavitated core layer, which may be the same as or different than the first microporous breathable cavitated core layer C 1
  • a 2 represents a second non-cavitated skin layer, which may be the same as or different than the first non-cavitated skin layer A 1 .
  • the first cavitated core layer 72 and/or the second cavitated core layer 76 contains polyethylene (e.g., metallocene polyethylene resin and/or low density polyethylene resin) and calcium carbonate. Additional adhesives, antioxidants, colorants, and/or processing aids may optionally be added.
  • the microporous breathable cavitated core layer C 1 may differ from the microporous breathable film cavitated core layer C 2 in the amount and/or identity of solid filler present (e.g., calcium carbonate, barium sulfate, talc, glass spheres, other inorganic particles, etc.).
  • the inner polar polymer layer B may contain a hygroscopic elastomer such as Dupont HYTREL PET and an adhesive such as Dupont BYNEL 3101 20% EVA or Dupont AC1820 acrylate, with additional antioxidants, colorants, and processing aids optionally being added.
  • the inner polar polymer layer B contains adhesive and about 50% by weight or more of hygroscopic elastomer.
  • hygroscopic polymers such as ⁇ -caprolactone, polyester block amides, polyester elastomers, polyamides, and blends thereof may be utilized as the inner polar polymer layer.
  • Multi-layer non-breathable films 68 of a type described above are not limited to any specific kind of film structure.
  • Other film structures may likewise achieve the same or a similar result as the three-layer film 56 shown in FIG. 7 or the five-layer structure A-C-B-C-A shown in FIG. 9 .
  • Film structure is a function of equipment design and capability. For example, the number of layers in a film depends only on the technology available and the desired end use for the film.
  • A represents a non-cavitated skin layer (e.g., 13, 58, 60, 59, 61, 70, and/or 74)
  • C represents a microporous, breathable cavitated core layer (e.g., 3, 62, 63, 72, 76, and/or 82):
  • each of the microporous breathable cavitated core layers C may include two or more microporous breathable film layers in order to better control other film properties, such as the ability to bond to nonwovens.
  • some exemplary film structures include but are not limited to the following:
  • an ABA structure may be multiplied from about 10 to about 1000 times.
  • the resulting 10-time multiplied ABA structure may be expressed as follows:
  • the compositions used to extrude cavitated core layers contain a solid filler.
  • the cavitated core layers upon stretching, the cavitated core layers becomes microporous and breathable.
  • non-cavitated skin layers e.g., 13, 58, 60, 59, 61, 70, and/or 74
  • the thickness and composition of one or more skin layers of a multi-layer film in accordance with the present disclosure may be selected so that when the precursor film is subsequently stretched, the resulting film is breathable.
  • a pair of skin layers sandwiching a core layer may be relatively thin and together account for no more than about 30% of the total film thickness.
  • the skin layer may still be breathable.
  • the skin layer may include one or more discontinuities that are introduced during the stretching process. The likelihood of discontinuities forming in a skin layer may increase as the thickness of the skin layer subjected to stretching decreases.
  • a multi-layer partially-breathable film 80 may be provided.
  • the multi-layer partially-breathable film 80 contains at least one cavitated core layer 82 and at least one skin layer 84 .
  • the cavitated core layer 82 contains one or a plurality of polyolefins and one or a plurality of inorganic fillers.
  • the skin layer 84 includes one or a plurality of polyolefins, which may be the same as or different than the polyolefins of the cavitated core layer 82 , and further includes one or a plurality of discontinuities 86 . Due to the discontinuity 86 present in skin layer 84 , the multi-layer partially-breathable film 80 has a microporous breathable region 88 and a non-microporous, non-breathable region 90 .
  • the multi-layer partially-breathable film 80 may be formed, for example, by applying a surface modification technique, including but not limited to corona treatment, to the pre-stretched film.
  • the surface modification technique may be used to treat regions of the pre-stretched film that are intended to become breathable, such that the film will be configured to break in the treated regions once it is subjected to stretching.
  • a multi-layer partially-breathable film 80 may be formed by selectively applying CD-IMG stretching more aggressively to certain regions of the film (e.g., particular lanes) that are intended to become breathable.
  • portions of the quenched film that were previously subjected to selective cross-directional stretching may become breathable upon further downweb stretching in the machine direction, whereas portions of the quenched film that did not previously receive prior cross-directional stretching (or received less aggressive cross-directional stretching) may be configured to remain non-breathable even after being subjected to downweb machine direction stretching.
  • a multi-layer film e.g., 2
  • a multi-layer non-breathable film e.g., 56, 64, and/or 68
  • a multi-layer partially-breathable film e.g. 80
  • films in accordance with the present disclosure may be laminated to a fabric, scrim, or other film support by thermal, ultrasonic, and/or adhesive bonding. The support may be attached to at least one face of the film and or to both faces of the film.
  • the laminate may be made using wovens, knits, nonwovens, paper, netting, or other films. Adhesive bonding may be used to prepare such laminates. Adhesive bonding may be performed with adhesive agents such as powders, adhesive webs, liquid, hot-melt and solvent-based adhesives. Additionally, these types of support may be used with ultrasonic or thermal bonding if the polymers in the support are compatible with the film surface. Laminates of the present multilayer films and nonwoven fabrics may provide surgical barriers. In one example, the fabrics are spunbonded or spunbond-meltblown-spunbond (SMS) fabrics. In another example, the fabrics may be spunlaced, airlaid, powder-bonded, thermal-bonded, or resin-bonded. The encasing of the polar polymer layer 78 protects the polar polymer layer 78 from mechanical damage or thermal damage and allows for thermal and ultrasonic bonding of the multilayer film at extremely low thicknesses.
  • adhesive agents such as powders, adhesive webs, liquid, hot-melt and solvent
  • a personal hygiene product in accordance with the present disclosure includes at least one inner multi-layer film (e.g., 2, 56, 64, 68, and/or 80) prepared by a process as described above and at least one outer non-woven layer. At least one non-cavitated skin layer of a multi-layer film in accordance with the present disclosure is configured for attachment to and/or bonding with the outer non-woven layer.
  • the personal hygiene product further includes at least one polar polymer layer 78 disposed between a pair of non-cavitated skin layers, as shown in FIG. 9 .
  • the at least one non-cavitated skin layer of a multi-layer film in accordance with the present disclosure is bonded to the at least one outer non-woven layer without an adhesive (e.g., via heat sealing, ultrasonic welding, and/or the like).
  • each of the at least one non-cavitated skin layer and the at least one outer non-woven layer includes polypropylene and/or polyethylene.
  • each of the at least one non-cavitated skin layer and the at least one outer non-woven layer includes polypropylene.
  • the personal hygiene product in accordance with the present disclosure is configured as an incontinence brief, a diaper, a surgical gown, or a feminine hygiene product.
  • a multi-layer film in accordance with the present disclosure may be used as an ultrathin backsheet (e.g., for a diaper).
  • Functions of a diaper backsheet may include one or more of the following: (a) provide a barrier to liquid and solid waste (e.g., through the use of absorbent cores, which typically contain superabsorbent polymers); (b) provide a barrier to odor; (c) provide opacity to mask soiling (e.g., by loading a polymeric layer of the diaper backsheet with TiO 2 ); and (d) be able to carry print and/or artwork.
  • superabsorbent polymers are typically sharp-cornered particles with a tendency to rupture backsheets under compressive pressure or when dragged at a different speed from the barrier film.
  • SAPs superabsorbent polymers
  • the challenge increases with decreasing film thickness since the proportion of TiO 2 in the blend grows higher with any thickness decrease, and the TiO 2 adds cost and detracts from desired properties.
  • diaper backsheets have typically been embossed in order to better simulate a cloth-like appearance.
  • diaper backsheets nowadays are covered with a non-woven material, and an emboss pattern no longer serves its original purpose.
  • a chill cast quenching process in accordance with the present teachings may be used to prepare a microporous breathable film (a.k.a. a cavitated film) that has a thickness of as low as about 0.28 mils (about 6.7 gsm) and yet exceptionally good puncture strength.
  • a microporous breathable film a.k.a. a cavitated film
  • an ultrathin diaper backsheet exhibiting good puncture resistance to SAP particles may be prepared by bonding a simple non-woven layer to a multi-layer non-breathable film in accordance with the present disclosure (i.e., a multi-layer non-breathable film prepared by a chill cast quenching process of a type described herein).
  • cavitation may serve as an alternative opacification aid to reduce or eliminate reliance on TiO 2 for masking diaper fouling.
  • the at least one cavitated core layer e.g., 3, 62, 63, 72, 76, and/or 82
  • present in a multi-layer film in accordance with the present teachings may thus be used to provide a low-cost alternative to opacification.
  • a microporous breathable layer e.g., a cavitated core layer
  • a microporous breathable layer may be turned off or otherwise reduced (e.g., by attaching the cavitated core layer to at least one non-cavitated skin layer).
  • an ultrathin backsheet in accordance with the present disclosure may resemble the multi-layer non-breathable film 56 shown in FIG. 7 .
  • an ultrathin backsheet in accordance with the present disclosure may resemble the multi-layer structure 64 shown in FIG. 8 . Since non-woven materials such as the non-woven layer 66 in FIG. 8 are typically polypropylene-based, the first non-cavitated skin layer 58 and the second non-cavitated skin layer 60 shown in FIG. 7 (also, the first non-cavitated skin layer 59 and the second non-cavitated skin layer 66 shown in FIG.
  • a multi-layer film having non-filled non-cavitated skin layers will be more compatible with ultrasonic bonding than an analogous microporous layer that contains mineral filler at the surface or just beneath a thin non-breathable skin layer.
  • a multi-layer non-breathable film 56 as shown in FIG. 7 having a polypropylene-based first non-cavitated skin layer 58 and a polypropylene-based second non-cavitated skin layer 60 feels softer to the touch and is quieter than a similar polypropylene-based film that does not contain at least one cavitated core layer 62 .
  • the cavitations present in the at least one cavitated core layer 62 confer the increased softness and quietness properties to multi-layer non-breathable films in accordance with the present disclosure. Both softness and quietness may be desirable attributes for applications such as diaper backsheets, incontinence briefs, and the like.
  • each of the first non-cavitated skin layer 58 and the second non-cavitated skin layer 60 shown in FIG. 7 contains polypropylene (e.g., homopolymer, impact copolymer).
  • the first non-cavitated skin layer 58 and the second non-cavitated skin layer 60 are comprised primarily of polypropylene (e.g., in some embodiments, greater than about 50 wt. %, 55 wt. %, 60 wt. %, 65 wt. %, 70 wt. %, 75 wt. %, 80 wt. %, 85 wt. %, 90 wt. %, 95 wt.
  • the first non-cavitated skin layer 58 and the second non-cavitated skin layer 60 consist essentially of polypropylene. In illustrative embodiments, at least one of the first non-cavitated skin layer 58 and the second non-cavitated skin layer 60 is non-filled. In some embodiments, both of the first non-cavitated skin layer 58 and the second non-cavitated skin layer 60 are non-filled.
  • the at least one cavitated core layer 62 shown in FIG. 7 contains a polyolefin (e.g., polyethylene and/or polypropylene), CaCO 3 filler and, optionally, a minimal amount of TiO 2 (e.g., in order to achieve a desired opacity at minimum cost). Since breathability per se is not a desired property in this application, a lower grade of CaCO 3 may be used in place of the higher grades that may be preferable when breathability is a goal in and of itself).
  • the multi-layer film 56 in FIG. 7 may be subjected to crossweb CD-IMG orientation to cavitate the core layer 62 and then to downweb MD stretch to add tensile strength for converting.
  • a backsheet film may also be useful to include a layer that is highly impermeable to odorants.
  • Polar molecules e.g., nylon, EVOH, PET
  • polar molecules may be used as described above in relation to FIG. 9 . If such polar molecules are used, there are advantages to not using them as exterior layers since the polar molecules are less compatible thermally or adhesively with the polyolefins commonly used in disposable products.
  • these hydrophilic polymers may create extrusion problems when present on a film exterior.
  • a central non-breathable layer may be selected for toughness, stiffness, or thermal resistance properties, and there may be advantages with respect to curl or other processing issues in keeping such layers internal. If structures are made with hydrophobic and hydrophilic materials, tie adhesives may be blended in or co-extruded as tie layers.
  • an extrusion cast line with up to 3 extruders was used.
  • the “A” and “B” extruders are 21 ⁇ 2′′ in diameter, and the “C” extruder is 13 ⁇ 4′′ in diameter.
  • the extruders feed into a combining feedblock manufactured by Cloeren Corporation of Orange, Tex., which can layer the A, B and C extruder outputs in a variety of configurations.
  • the molten polymer proceeds into a monolayer cast die (manufactured by Cloeren) that is about 36′′ wide.
  • the die has an adjustable gap. For the samples described herein, the adjustable gap was maintained between 10 and 40 mils.
  • the molten polymer drops down to a chill roll.
  • the chill roll had an embossed pattern FST-250 which was engraved by Pamarco of Roselle, N.J. as their pattern P-2739.
  • the embossed pattern P-2739 is a square pattern (e.g., with lines nearly aligned with the Machine Direction) with 250 squares per inch and a depth of about 31 microns.
  • the roll itself has an 18′′ diameter with internal water cooling.
  • the engrave roll pattern may be replaced with other patterns that are shallow enough not to interfere with a vacuum box quench.
  • One alternative is a 40 Ra pattern (40 micro-inch average roughness) generated by a sand-blasting process on a chrome plated roll.
  • a skinned multi-layer backsheet film having a structure CBBBC was prepared from the formulation XC3-828-2300.0 shown in Table 1.
  • composition of the CaCO 3 -containing formulation (CF7414) listed in Table 1 is specified below in Table 2.
  • the molten web formed by extrusion of the composition XC3-828-2300.0 shown in Table 1 was quenched by a chill cast vacuum box process in accordance with the present disclosure on a 250T roll (1749.9 rpm setting).
  • two backsheet films having a structure ABBBA were prepared from a formulation XC3-828-2204.0 using a conventional embossing process.
  • composition of formulation XC3-828-2204.0 used in Comparative Examples A and B is shown below in Table 4.
  • the multi-layer non-breathable film in accordance with the present disclosure essentially matched the tensile strength at peak machine direction of a much thicker conventional embossed film (Comp. Ex. A).
  • the multi-layer non-breathable film in accordance with the present disclosure also exhibited higher tensile strength at 5% strain machine direction and substantially higher secant modulus machine direction (1%) than the much thicker conventional embossed film (Comp. Ex. A).
  • the multi-layer non-breathable film in accordance with the present disclosure (Ex. 1) exhibited a Dart Impact Strength that was greater than that of the much thicker conventional embossed film (Comp. Ex. A).
  • microporous breathable films prepared by a conventional embossing process typically include LDPE to assist in the processing.
  • the LDPE may be omitted, thereby affording stronger films having properties that were heretofore unachievable with conventional films.

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Abstract

Multi-layer films include at least one cavitated core layer that is microporous and breathable, and at least one skin layer. The cavitated core layer includes a polyolefin and an inorganic filler dispersed in the polyolefin. Methods for forming polymeric films and articles of manufacture prepared therefrom are described.

Description

PRIORITY CLAIM
This application claims priority under 35 U.S.C. § 119(e) to U.S. Provisional Application Ser. No. 62/251,415, filed Nov. 5, 2015, which is expressly incorporated by reference herein.
BACKGROUND
The present disclosure relates to polymeric materials, and particularly to polymeric films. More particularly, the present disclosure relates to multi-layer polymeric films having a microporous core layer formed from polymeric material and filler.
SUMMARY
According to the present disclosure, a multi-layer non-breathable film is made using a manufacturing process. The manufacturing process comprises the steps of extruding a composition to form a molten web, casting the molten web to form a quenched film, and stretching the quenched film to form the microporous breathable film.
In illustrative embodiments, two or more extrudable materials are co-extruded to form the molten web. The quenched film is formed from the molten web by casting the molten web against a surface of a chill roll using a vacuum box and/or blowing air (e.g., an air knife and/or an air blanket).
In illustrative embodiments, a multi-layer film in accordance with the present disclosure comprises at least one cavitated core layer and at least one non-cavitated skin layer. The at least one cavitated core layer is microporous and breathable. The at least one non-cavitated skin layer is non-microporous and non-breathable.
In illustrative embodiments, a multi-layer non-breathable film in accordance with the present disclosure comprises first and second non-cavitated skin layers, at least one cavitated core layer disposed between the first and second non-cavitated skin layers, and at least one polar polymer layer disposed between the first and second non-cavitated skin layers. The at least one polar polymer layer comprises a hygroscopic polymer.
In illustrative embodiments, a partially breathable multi-layer film in accordance with the present disclosure comprises at least one cavitated core layer and at least one skin layer having one or a plurality of discontinuities therein. The multi-layer film includes at least one microporous breathable region and at least one non-microporous non-breathable region.
In illustrative embodiments, a personal hygiene product comprises at least one inner multi-layer film in accordance with the present disclosure and at least one outer non-woven layer. At least a portion of a non-cavitated skin layer of the inner multi-layer film is bonded to at least a portion of the outer non-woven layer.
Additional features of the present disclosure will become apparent to those skilled in the art upon consideration of illustrative embodiments exemplifying the best mode of carrying out the disclosure as presently perceived.
BRIEF DESCRIPTIONS OF THE DRAWINGS
The detailed description particularly refers to the accompanying figures in which:
FIG. 1 is a diagrammatic view of a representative embodiment of a multi-layer film that includes two layers;
FIG. 2 is a diagrammatic view of an exemplary process for machine direction (MD) stretching of a polymeric film;
FIG. 3 is a diagrammatic view of an exemplary process for cross-directional (CD) stretching of a polymeric film;
FIG. 4 is a diagrammatic view of an exemplary process for intermeshing gears (IMG) stretching of a polymeric film;
FIG. 5 is a diagrammatic view of an exemplary process for casting a molten web against a chill roll using a vacuum box;
FIG. 6 is a diagrammatic view of an exemplary process for casting a molten web against a chill roll using an air knife;
FIG. 7 is a diagrammatic view of a representative embodiment of a multi-layer non-breathable film that includes three layers;
FIG. 8 is a diagrammatic view of a representative embodiment of a multi-layer non-breathable film bonded to a non-woven material;
FIG. 9 is a diagrammatic view of a representative embodiment of a multi-layer non-breathable film that includes five layers; and
FIG. 10 is a diagrammatic view of a representative embodiment of a multi-layer partially-breathable film that includes two layers.
DETAILED DESCRIPTION
A first embodiment of a multi-layer film 2 in accordance with the present disclosure is shown, for example, in FIG. 1. The multi-layer film 2 includes a cavitated core layer 3 and a non-cavitated skin layer 13. The cavitated core layer 3 includes a thermoplastic polymer 4 and a solid filler 6 dispersed in the thermoplastic polymer 4. In some embodiments, the cavitated core layer 3 includes a combination of two or more thermoplastic polymers 4 and/or a combination of two or more solid fillers 6. The non-cavitated skin layer 13 contains a thermoplastic polymer (e.g., which may be the same as or different than the thermoplastic polymer 4 in the cavitated core layer 3). In some embodiments, the non-cavitated skin layer 13 includes a combination of two or more thermoplastic polymers 4.
As shown in FIG. 1, the cavitated core layer 3 includes an interconnected network of micropores 8 formed in the thermoplastic polymer resin 4. On average, the micropores 8 are smaller in size than the size of a typical water droplet but larger in size than a water vapor molecule. As a result, the micropores 8 permit the passage of water vapor but minimize or block the passage of liquid water. Two representative pathways for the transmission of water vapor through the cavitated core layer 3 are shown by the dashed lines 10 and 12 in FIG. 1.
A precursor film containing at least one cavitated core layer 3 (e.g., containing a thermoplastic polymer 4 and a solid filler 6 dispersed in the thermoplastic polymer 4) and at least one non-cavitated skin layer 13 (e.g., containing a thermoplastic polymer 4) may be produced by either a cast film process or a blown film process. The film thus produced may then be stretched by one or more stretching processes. The stretching process moves (e.g., pulls) polymeric material away from the surface of solid filler dispersed therein, thereby forming the micropores 8.
In one example, stretching may be achieved via machine direction (MD) orientation by a process analogous to that shown in simplified schematic form in FIG. 2. For example, the film 14 shown in FIG. 2 may be passed between at least two pairs of rollers in the direction of an arrow 15. In this example, first roller 16 and a first nip 20 run at a slower speed (V1) than the speed (V2) of a second roller 18 and a second nip 22. The ratio of V2/V1 determines the degree to which the film 14 is stretched. Since there may be enough drag on the roll surface to prevent slippage, the process may alternatively be run with the nips open. Thus, in the process shown in FIG. 2, the first nip 20 and the second nip 22 are optional.
In another example, stretching may be achieved via transverse or cross-directional (CD) stretching by a process analogous to that shown in simplified schematic form in FIG. 3. For example, the film 24 shown in FIG. 3 may be moved in the direction of the arrow 28 while being stretched sideways on a tenter frame in the directions of doubled-headed arrow 30. The tenter frame includes a plurality of attachment mechanisms 26 configured for gripping the film 24 along its side edges.
In a further example, stretching may be achieved via intermeshing gears (IMG) stretching by a process analogous to the one shown in simplified schematic form in FIG. 4. For example, a film 32 may be moved between a pair of grooved or toothed rollers as shown in FIG. 4 in the direction of arrow 33. In one example, the first toothed roller 34 may be rotated in a clockwise direction while the second toothed roller 36 may be rotated in a counterclockwise direction. At each point at which one or more teeth of the rollers 34 and 36 contact the film 32, localized stresses may be applied that stretch the film 32 and introduce interconnecting micropores therein analogous to the micropores 8 shown in FIG. 1. By the use of IMG stretching, the film 32 may be stretched in the machine direction (MD), the cross direction (CD), at oblique angles to the MD, or in any combination thereof.
A precursor film containing at least one cavitated core layer 3 (e.g., containing a thermoplastic polymer 4 and a solid filler 6 dispersed in the thermoplastic polymer 4) and at least one non-cavitated skin layer 13 (e.g., containing a thermoplastic polymer 4) may be stretched to form a multi-layer film 2 in accordance with the present disclosure. The precursor film may be prepared by mixing together the thermoplastic polymer 4 (or a combination of thermoplastic polymers 4), the solid filler 6 (or a combination of solid fillers 6), and any optional components until blended, heating the mixture, and then co-extruding the heated mixture with at least one additional extrudable material to form a molten web. The at least one additional extrudable material may contain a thermoplastic polymer 4 (or a combination of thermoplastic polymers 4). A suitable film-forming process may be used to form a precursor film en route to forming a multi-layer film. For example, the precursor film may be manufactured by casting or extrusion using blown-film, co-extrusion, or single-layer extrusion techniques and/or the like. In one example, the precursor film may be wound onto a winder roll for subsequent stretching in accordance with the present disclosure. In another example, the precursor film may be manufactured in-line with a film stretching apparatus such as shown in one or more of FIGS. 2-4.
In addition to containing one or more thermoplastic polymers and one or more solid fillers, the precursor film may also contain other optional components to improve the film properties or processing of the film. Representative optional components include but are not limited to anti-oxidants (e.g., added to prevent polymer degradation and/or to reduce the tendency of the film to discolor over time) and processing aids (e.g., added to facilitate extrusion of the precursor film). In one example, the amount of one or more anti-oxidants in the precursor film is less than about 1% by weight of the film and the amount of one or more processing aids is less than about 5% by weight of the film. Additional optional additives include but are not limited to whitening agents (e.g., titanium dioxide), which may be added to increase the opacity of the film. In one example, the amount of one or more whitening agents is less than about 10% by weight of the film. Further optional components include but are not limited to antiblocking agents (e.g., diatomaceous earth) and slip agents (e.g. erucamide a.k.a. erucylamide), which may be added to allow film rolls to unwind properly and to facilitate secondary processing (e.g., diaper making). In one example, the amount of one or more antiblocking agents and/or one or more slip agents is less than about 5% by weight of the film. Further additional optional additives include but are not limited to scents, deodorizers, pigments other than white, noise reducing agents, and/or the like, and combinations thereof. In one example, the amount of one or more scents, deodorizers, pigments other than white, and/or noise reducing agents is less than about 10% by weight of the film.
Prior to stretching, the precursor film may have an initial basis weight of less than about 100 grams per square meter (gsm). In one example, the precursor film has an initial basis weight of less than about 75 gsm.
In one example, a multi-layer film 2 in accordance with the present disclosure is formed via a blown film process. In another example, a multi-layer film 2 in accordance with the present disclosure is formed via a cast film process. The cast film process involves the extrusion of molten polymers through an extrusion die to form a thin film. The film is pinned to the surface of a chill roll with an air knife, an air blanket, and/or a vacuum box.
In illustrative embodiments, a process for making a multi-layer film 2 in accordance with the present disclosure includes (a) extruding two or more extrudable materials to form a molten web, wherein at least one of the two or more extrudable materials comprises a first polyolefin and an inorganic filler, and at least another of the two or more extrudable materials comprises a second polyolefin, (b) casting the molten web against a surface of a chill roll using an air knife, an air blanket, a vacuum box, or a combination thereof to form a quenched film, and (c) stretching the quenched film to form the multi-layer film 2. The first olefin and the second olefin may be the same or different.
It has been discovered that by using a vacuum box, blowing air (e.g., an air knife and/or an air blanket), or a vacuum box in combination with blowing air to cast the molten web against a chill roll in accordance with the present disclosure, a cavitated core layer 3 exhibiting surprisingly and unexpectedly improved properties as compared to other microporous breathable films may be prepared. As further described below, these properties may include reduced basis weight, increased strain at peak machine direction, increased tensile strength at peak machine direction, increased tensile strength at 5% strain machine direction, increased secant modulus machine direction (1%), increased Dart Impact Strength, and/or the like, and combinations thereof.
In one example, the molten web is cast against the surface of the chill roll under negative pressure using a vacuum box as shown in simplified schematic form in FIG. 5. A vacuum box works by evacuating air between the film and the surface of the chill roll. For example, as shown in FIG. 5, a film 46 is extruded from an extrusion die 40 in the direction of arrow 47 and quenched from the molten state with a vacuum box 42. The vacuum box 42 draws a vacuum behind the molten web 46 in the direction of arrow 44 to draw the film 46 down onto the chill roll 38. The vacuum drawn in the direction of arrow 44 removes the entrained air between the surface of the chill roll 38 and the film 46. The vacuum box process is not subject to draw resonance for high molecular weight polymers that would tend to extrude unstable thickness in a nipped quench process due to the draw resonance phenomenon.
When a vacuum box 42 is used, the molten polymer may exit the die 40 and hit the chill roll 38 within a smaller distance than in an embossed process. For example, in some embodiments, the melt curtain is configured to hit the chill roll 38 within a distance of less than about 12 inches, 11 inches, 10 inches, 9 inches, 8 inches, 7 inches, 6 inches, 5 inches, 4 inches, 3, inches, 2 inches, or 1 inch. In illustrative embodiments, the melt curtain is configured to exit the die and hit the roll within a distance of less than about 3 inches and, in some examples, within a distance of about or less than 1 inch. One advantage of reducing the distance between the die 40 and the roll surface 38 as compared to in a nipped quench process is that smaller distances are less susceptible to the phenomenon of neck-in. Neck-in refers to a reduction in width of the molten web that occurs as the web leaves the die. By drawing the film 46 onto a surface of the chill roll 38 over a short distance as shown in FIG. 5, the vacuum box 42 may enhance web cooling, facilitate higher line speeds, reduce film neck-in, and/or reduce drag at the lip exit.
In another example, the molten web is cast against the surface of the chill roll under positive pressure using an air knife or air blanket, as shown in simplified schematic form in FIG. 6. An air knife works to promote web quenching by gently blowing a high-velocity, low-volume air curtain over the molten film, thereby pinning the molten film to the chill roll for solidification. For example, as shown in FIG. 6, a film 54 is extruded from an extrusion die 50 in the direction of arrow 55 and quenched from the molten state with an air knife 52 blowing an air curtain over the molten film 54, thereby pinning the molten web 54 against a surface of the chill roll 48. An air blanket (also called a soft box) works similarly to an air knife and promotes web quenching by gently blowing an air curtain over the molten film. However, in the case of an air blanket, the air curtain is low velocity and high volume.
In a further example, the molten web is cast against the surface of the chill roll under a combination of negative pressure from a vacuum box, as shown in FIG. 5, and positive pressure from an air knife, as shown in FIG. 6. In illustrative embodiments, in the casting of the molten web against a surface of the chill roll, an exit temperature of cooling fluid passing through the chill roll is between about 50 degrees Fahrenheit and about 130 degrees Fahrenheit and, in some examples, between about 75 degrees Fahrenheit and about 130 degrees Fahrenheit.
The thermoplastic polymer 4 (or combination of thermoplastic polymers 4) used to make a non-cavitated skin layer 13 and/or a cavitated core layer 3 of a multi-layer film 2 in accordance with the present disclosure is not restricted, and may include all manner of thermoplastic polymers. In illustrative embodiments, the thermoplastic polymer is a polyolefin, including but not limited to homopolymers, copolymers, terpolymers, and/or blends thereof.
Representative polyolefins that may be used in accordance with the present disclosure include but are not limited to low density polyethylene (LDPE), high density polyethylene (HDPE), linear low density polyethylene (LLDPE), ultra-low density polyethylene (ULDPE), polypropylene, ethylene-propylene copolymers, polymers made using a single-site catalyst, ethylene maleic anhydride copolymers (EMAs), ethylene vinyl acetate copolymers (EVAs), polymers made using Zeigler-Natta catalysts, styrene-containing block copolymers, and/or the like, and combinations thereof. Methods for manufacturing LDPE are described in The Wiley Encyclopedia of Packaging Technology, pp. 753-754 (Aaron L. Brody et al. eds., 2nd Ed. 1997) and in U.S. Pat. No. 5,399,426, both of which are incorporated by reference herein, except that in the event of any inconsistent disclosure or definition from the present specification, the disclosure or definition herein shall be deemed to prevail.
ULDPE may be produced by a variety of processes, including but not limited to gas phase, solution and slurry polymerization as described in The Wiley Encyclopedia of Packaging Technology, pp. 748-50 (Aaron L. Brody et al. eds., 2nd Ed. 1997), incorporated by reference above, except that in the event of any inconsistent disclosure or definition from the present specification, the disclosure or definition herein shall be deemed to prevail.
ULDPE may be manufactured using a Ziegler-Natta catalyst, although a number of other catalysts may also be used. For example, ULDPE may be manufactured with a metallocene catalyst. Alternatively, ULDPE may be manufactured with a catalyst that is a hybrid of a metallocene catalyst and a Ziegler-Natta catalyst. Methods for manufacturing ULDPE are also described in U.S. Pat. Nos. 5,399,426, 4,668,752, 3,058,963, 2,905,645, 2,862,917, and 2,699,457, each of which is incorporated by reference herein in its entirety, except that in the event of any inconsistent disclosure or definition from the present specification, the disclosure or definition herein shall be deemed to prevail. The density of ULDPE is achieved by copolymerizing ethylene with a sufficient amount of one or more monomers. In illustrative embodiments, the monomers are selected from 1-butene, 1-hexene, 4-methyl-1-pentene, 1-octene, and combinations thereof. Methods for manufacturing polypropylene are described in Kirk-Othmer Concise Encyclopedia of Chemical Technology, pp. 1420-1421 (Jacqueline I. Kroschwitz et al. eds., 4th Ed. 1999), which is incorporated herein by reference, except that in the event of any inconsistent disclosure or definition from the present specification, the disclosure or definition herein shall be deemed to prevail.
In illustrative embodiments, a polyolefin for use in accordance with the present disclosure includes polyethylene, polypropylene, or a combination thereof. In one example, the polyethylene includes linear low density polyethylene which, in some embodiments, includes a metallocene polyethylene. In another example, the polyethylene includes a combination of linear low density polyethylene and low density polyethylene. In a further example, the polyolefin consists essentially of only linear low density polyethylene.
In addition to thermoplastic polymer (e.g., polyolefin), an extrudable material to be extruded in accordance with the present disclosure may further include a solid filler. The solid filler is not restricted, and may include all manner of inorganic or organic materials that are (a) non-reactive with thermoplastic polymer, (b) configured for being uniformly blended and dispersed in the thermoplastic polymer, and (c) configured to promote a microporous structure within the film when the film is stretched. In illustrative embodiments, the solid filler includes an inorganic filler.
Representative inorganic fillers for use in accordance with the present disclosure include but are not limited to sodium carbonate, calcium carbonate, magnesium carbonate, barium sulfate, magnesium sulfate, aluminum sulfate, magnesium oxide, calcium oxide, alumina, mica, talc, silica, clay (e.g., non-swellable clay), glass spheres, titanium dioxide, aluminum hydroxide, zeolites, and a combination thereof. In illustrative embodiments, the inorganic filler includes an alkali metal carbonate, an alkaline earth metal carbonate, an alkali metal sulfate, an alkaline earth metal sulfate, or a combination thereof. In one example, the inorganic filler includes calcium carbonate.
In another example, the solid filler includes a polymer (e.g., high molecular weight high density polyethylene, polystyrene, nylon, blends thereof, and/or the like). The use of polymer fillers creates domains within the thermoplastic polymer matrix. These domains are small areas, which may be spherical, where only the polymer filler is present as compared to the remainder of the thermoplastic matrix where no polymer filler is present. As such, these domains act as particles.
The solid filler 6 provided in a composition to be extruded in accordance with the present disclosure may be used to produce micropores 8 of multi-layer film 2, as shown in FIG. 1. The dimensions of the solid filler 6 particles may be varied based on a desired end use (e.g., the desired properties of cavitated core layer 3). In one example, the average particle size of a solid filler particle ranges from about 0.1 microns to about 15 microns. In illustrative embodiments, the average particle size ranges from about 1 micron to about 5 microns and, in some examples, from about 1 micron to about 3 microns. The average particle size may be one of several different values or fall within one of several different ranges. For example, it is within the scope of the present disclosure to select an average particle size of the solid filler to be one of the following values: about 0.1 microns, 0.2 microns, 0.3 microns, 0.4 microns, 0.5 microns, 0.6 microns, 0.7 microns, 0.8 microns, 0.9 microns, 1.0 microns, 1.1 microns, 1.2 microns, 1.3 microns, 1.4 microns, 1.5 microns, 1.6 microns, 1.7 microns, 1.8 microns, 1.9 microns, 2.0 microns, 2.1 microns, 2.2 microns, 2.3 microns, 2.4 microns, 2.5 microns, 2.6 microns, 2.7 microns, 2.8 microns, 2.9 microns, 3.0 microns, 3.5 microns, 4.0 microns, 4.5 microns, 5.0 microns, 5.5 microns, 6.0 microns, 6.5 microns, 7.0 microns, 7.5 microns, 8.0 microns, 8.5 microns, 9.0 microns, 9.5 microns. 10.0 microns, 10.5 microns, 11.0 microns, 11.5 microns, 12.0 microns, 12.5 microns, 13.0 microns, 13.5 microns, 14.0 microns, 14.5 microns, or 15.0 microns.
It is also within the scope of the present disclosure for the average particle size of the solid filler 6 provided in a composition to be extruded in accordance with the present disclosure to fall within one of many different ranges. In a first set of ranges, the average particle size of the solid filler 6 is in one of the following ranges: about 0.1 microns to 15 microns, 0.1 microns to 14 microns, 0.1 microns to 13 microns, 0.1 microns to 12 microns, 0.1 microns to 11 microns, 0.1 microns to 10 microns, 0.1 microns to 9 microns, 0.1 microns to 8 microns, 0.1 microns to 7 microns, 0.1 microns to 6 microns, 0.1 microns to 5 microns, 0.1 microns to 4 microns, and 0.1 microns to 3 microns. In a second set of ranges, the average particle size of the solid filler 6 is in one of the following ranges: about 0.1 microns to 5 microns, 0.2 microns to 5 microns, 0.3 microns to 5 microns, 0.4 microns to 5 microns, 0.5 microns to 5 microns, 0.6 microns to 5 microns, 0.7 microns to 5 microns, 0.8 microns to 5 microns, 0.9 microns to 5 microns, and 1.0 microns to 5 microns. In a third set of ranges, the average particle size of the solid filler 6 is in one of the following ranges: about 0.1 microns to 4.9 microns, 0.2 microns to 4.8 microns, 0.3 microns to 4.7 microns, 0.4 microns to 4.6 microns, 0.5 microns to 4.5 microns, 0.6 microns to 4.4 microns, 0.7 microns to 4.3 microns, 0.8 microns to 4.2 microns, 0.9 microns to 4.1 microns, and 1.0 microns to 4.0 microns.
In illustrative embodiments, the amount of solid filler used in accordance with the present disclosure includes from about 30% by weight to about 75% by weight of the material to be extruded, quenched film formed from the extrusion of two or more extrudable materials, and/or multi-layer film formed from the quenched film. In further illustrative embodiments, the amount of solid filler used in accordance with the present disclosure includes from about 50% by weight to about 75% by weight of the material to be extruded, quenched film formed from the extrusion of two or more extrudable materials, and/or multi-layer film formed from the quenched film. Although amounts of filler outside this range may also be employed, an amount of solid filler that is less than about 30% by weight may not be sufficient to impart uniform breathability to a film. Conversely, amounts of filler greater than about 75% by weight may be difficult to blend with the polymer and may cause a loss in strength in the final film.
The amount of solid filler 6 may be varied based on a desired end use (e.g., the desired properties of the cavitated core layer 3). In one example, the amount of solid filler 6 ranges from about 40% to about 60% by weight of the material to be extruded, quenched film formed from the extrusion of the two or more extrudable materials, and/or multi-layer film formed from the quenched film. In another example, the amount of solid filler 6 ranges from about 45% to about 55% by weight of the material to be extruded, quenched film formed from the extrusion of the two or more extrudable materials, and/or multi-layer film formed from the quenched film. The amount of solid filler 6 may be one of several different values or fall within one of several different ranges. For example, it is within the scope of the present disclosure to select an amount of the solid filler 6 to be one of the following values: about 30%, 31%, 32%, 33%, 34%, 35%, 36%, 37%, 38%, 39%, 40%, 41%, 42%, 43%, 44%, 45%, 46%, 47%, 48%, 49%, 50%, 51%, 52%, 53%, 54%, 55%, 56%, 57%, 58%, 59%, 60%, 61%, 62%, 63%, 64%, 65%, 66%, 67%, 68%, 69%, 70%, 71%, 72%, 73%, 74%, or 75% by weight of the material to be extruded, quenched film formed from the extrusion of the two or more extrudable materials, and/or multi-layer film formed from the quenched film.
It is also within the scope of the present disclosure for the amount of the solid filler 6 to fall within one of many different ranges. In a first set of ranges, the amount of the solid filler 6 is in one of the following ranges: about 31% to 75%, 32% to 75%, 33% to 75%, 34% to 75%, 35% to 75%, 36% to 75%, 37% to 75%, 38% to 75%, 39% to 75%, 40% to 75%, 41% to 75%, 42% to 75%, 43% to 75%, 44% to 75%, and 45% to 75% by weight of the material to be extruded, quenched film formed from the extrusion of the two or more extrudable materials, and/or multi-layer film formed from the quenched film. In a second set of ranges, the amount of the solid filler is in one of the following ranges: about 30% to 74%, 30% to 73%, 30% to 72%, 30% to 71%, 30% to 70%, 30% to 69%, 30% to 68%, 30% to 67%, 30% to 66%, 30% to 65%, 30% to 64%, 30% to 63%, 30% to 62%, 30% to 61%, 30% to 60%, 30% to 59%, 30% to 58%, 30% to 57%, 30% to 56%, 30% to 55%, 30% to 54%, 30% to 53%, 30% to 52%, 30% to 51%, 30% to 50%, 30% to 49%, 30% to 48%, 30% to 47%, 30% to 46%, and 30% to 45% by weight of the material to be extruded, quenched film formed from the extrusion of the two or more extrudable materials, and/or multi-layer film formed from the quenched film. In a third set of ranges, the amount of the solid filler is in one of the following ranges: about 31% to 74%, 32% to 73%, 33% to 72%, 34% to 71%, 35% to 70%, 36% to 69%, 37% to 68%, 38% to 67%, 39% to 66%, 40% to 65%, 41% to 64%, 42% to 63%, 43% to 62%, 44% to 61%, 45% to 60%, 45% to 59%, 45% to 58%, 45% to 57%, 45% to 56%, and 45% to 55% by weight of the material to be extruded, quenched film formed from the extrusion of the two or more extrudable materials, and/or multi-layer film formed from the quenched film.
Although filler loading may be conveniently expressed in terms of weight percentages, the phenomenon of microporosity may alternatively be described in terms of volume percent of filler relative to total volume. By way of illustration, for calcium carbonate filler having a specific gravity of 2.7 g/cc and a polymer having a specific gravity of about 0.9, 35% by weight CaCO3 corresponds to a filler loading of about 15% by volume {(0.35/2.7)/(0.65/0.9+0.35/2.7)}. Similarly, the 75 weight percent upper end of the range described above corresponds to about 56% by volume of CaCO3. Thus, the amount of filler may be adjusted to provide comparable volume percentages for alternative solid fillers that have different (e.g., unusually low or high) specific gravities as compared to calcium carbonate.
In some embodiments, to render the solid filler particles free-flowing and to facilitate their dispersion in a polymeric material, the filler particles may be coated with a fatty acid and/or other suitable processing acid. Representative fatty acids for use in this context include but are not limited to stearic acid or longer chain fatty acids.
The type of stretching used to transform a quenched film into a multi-layer film 2 in accordance with the present disclosure is not restricted. All manner of stretching processes and combinations of stretching processes that are capable of moving (e.g., pulling) polymeric material 4 away from the surface of solid filler 6 dispersed therein in order to form micropores 8 in a cavitated core layer 3 are contemplated for use. In some examples, the stretching includes cross-directional stretching. In other examples, the stretching includes CD-IMG stretching. In further examples, the stretching includes MD stretching. In still further examples, the stretching includes MD IMG stretching. In additional examples, the stretching includes cold draw. In some embodiments, the stretching includes a combination of two or more different types of stretching including but not limited to MD stretching, CD IMG stretching, MD IMG stretching, cold draw, and/or the like. In some examples, the stretching includes a combination of CD IMG stretching and cold draw (which, in some embodiments, is performed subsequently to the CD IMG stretching). In illustrative embodiments, the stretching includes CD-IMG stretching followed by downweb MD stretching.
In illustrative embodiments, the type of stretching used to transform a quenched film into a multi-layer film 2 in accordance with the present disclosure includes CD IMG stretching. In addition, in illustrative embodiments, at least a portion of the stretching is performed at a temperature above ambient temperature. In one example, at least a portion of the stretching is performed at a temperature of between about 60 degrees Fahrenheit and about 200 degrees Fahrenheit.
In illustrative embodiments, a process for making a multi-layer film 2 in accordance with the present disclosure further includes annealing the multi-layer film 2. In one example, the annealing is performed at a temperature of between about 75 degrees Fahrenheit and about 225 degrees Fahrenheit.
In illustrative embodiments, as noted above, a multi-layer film 2 prepared in accordance with the present disclosure (e.g., by using a vacuum box and/or air knife to cast a molten web against a chill roll) may have reduced basis weight, increased tensile strength at peak machine direction, increased tensile strength at 5% strain machine direction, increased secant modulus machine direction (1%), and/or increased Dart Impact Strength as compared to conventional multi-layer films containing a microporous breathable layer.
The basis weight of a multi-layer film 2 in accordance with the present disclosure may be varied based on a desired end use (e.g., the desired properties and/or applications of the multi-layer film 2). In one example, the basis weight ranges from about 5 gsm to about 30 gsm. In another example, the basis weight ranges from about 6 gsm to about 25 gsm. In illustrative embodiments, the basis weight is less than about 14 gsm and, in some examples, less than about 12 gsm. Although basis weights outside this range may also be employed (e.g., basis weights above about 30 gsm), lower basis weights minimize material cost as well as maximize consumer satisfaction (e.g., a thinner film may provide increased comfort to the user of a personal hygiene product that includes the film). The basis weight of a multi-layer film 2 in accordance with the present disclosure may be one of several different values or fall within one of several different ranges. For example, it is within the scope of the present disclosure to select a basis weight to be one of the following values: about 30 gsm, 29 gsm, 28 gsm, 27 gsm, 26 gsm, 25 gsm, 24 gsm, 23 gsm, 22 gsm, 21 gsm, 20 gsm, 19 gsm, 18 gsm, 17 gsm, 16 gsm, 15 gsm, 14 gsm, 13 gsm, 12 gsm, 11 gsm, 10 gsm, 9 gsm, 8 gsm, 7 gsm, 6 gsm, or 5 gsm.
It is also within the scope of the present disclosure for the basis weight of the multi-layer film 2 to fall within one of many different ranges. In a first set of ranges, the basis weight of the multi-layer film 2 is in one of the following ranges: about 5 gsm to 30 gsm, 6 gsm to 30 gsm, 7 gsm to 30 gsm, 8 gsm to 30 gsm, 9 gsm to 30 gsm, 10 gsm to 30 gsm, 11 gsm to 30 gsm, 12 gsm to 30 gsm, 13 gsm to 30 gsm, and 14 gsm to 30 gsm. In a second set of ranges, the basis weight of the microporous breathable film is in one of the following ranges: about 5 gsm to 29 gsm, 5 gsm to 28 gsm, 5 gsm to 27 gsm, 5 gsm to 26 gsm, 5 gsm to 25 gsm, 5 gsm to 24 gsm, 5 gsm to 23 gsm, 5 gsm to 22 gsm, 5 gsm to 21 gsm, 5 gsm to 20 gsm, 5 gsm to 19 gsm, 5 gsm to 18 gsm, 5 gsm to 17 gsm, 5 gsm to 16 gsm, 5 gsm to 15 gsm, 5 gsm to 14 gsm, 5 gsm to 13 gsm, 5 gsm to 12 gsm, 5 gsm to 11 gsm, 5 gsm to 10 gsm, 5 gsm to 9 gsm, 5 gsm to 8 gsm, and 5 gsm to 7 gsm. In a third set of ranges, the basis weight of the multi-layer film 2 is in one of the following ranges: about 6 gsm to 29 gsm, 7 gsm to 29 gsm, 7 gsm to 28 gsm, 7 gsm to 27 gsm, 7 gsm to 26 gsm, 7 gsm to 25 gsm, 7 gsm to 24 gsm, 7 gsm to 23 gsm, 7 gsm to 22 gsm, 7 gsm to 21 gsm, 7 gsm to 20 gsm, 7 gsm to 19 gsm, 7 gsm to 18 gsm, 7 gsm to 17 gsm, 7 gsm to 16 gsm, 7 gsm to 15 gsm, 7 gsm to 14 gsm, 7 gsm to 13 gsm, 7 gsm to 12 gsm, 7 gsm to 11 gsm, and 7 gsm to 10 gsm.
In illustrative embodiments, a multi-layer film 2 in accordance with the present disclosure exhibits greater tensile strength at peak machine direction than conventional multi-layer films of similar basis weight. The basis weight of a multi-layer film 2 in accordance with the present disclosure may be varied based on a desired tensile strength at peak machine direction. In one example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a tensile strength at peak machine direction of at least about 500 grams/inch (g/in). In another example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a tensile strength at peak machine direction of at least about 600 grams/inch. In a further example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a tensile strength at peak machine direction of at least about 700 g/in. In a further example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a tensile strength at peak machine direction of at least about 800 g/in.
The tensile strength at peak machine direction of a multi-layer film 2 in accordance with the present disclosure may be one of several different values or fall within one of several different ranges. For example, for a multi-layer film having a basis weight of less than about 14 gsm—in some embodiments, less than about 13 gsm, 12 gsm, 11 gsm, or 10 gsm—it is within the scope of the present disclosure to select a tensile strength at peak machine direction to be greater than or equal to one of the following values: about 575 g/in, 576 g/in, 577 g/in, 578 g/in, 579 g/in, 580 g/in, 581 g/in, 582 g/in, 583 g/in, 584 g/in, 585 g/in, 586 g/in, 587 g/in, 588 g/in, 589 g/in, 590 g/in, 591 g/in, 592 g/in, 593 g/in, 594 g/in, 595 g/in, 596 g/in, 597 g/in, 598 g/in, 599 g/in, 600 g/in, 601 g/in, 602 g/in, 603 g/in, 604 g/in, 605 g/in, 606 g/in, 607 g/in, 608 g/in, 609 g/in, 610 g/in, 611 g/in, 612 g/in, 613 g/in, 614 g/in, 615 g/in, 616 g/in, 617 g/in, 618 g/in, 619 g/in, 620 g/in, 621 g/in, 622 g/in, 623 g/in, 624 g/in, 625 g/in, 626 g/in, 627 g/in, 628 g/in, 629 g/in, 630 g/in, 631 g/in, 632 g/in, 633 g/in, 634 g/in, 635 g/in, 636 g/in, 637 g/in, 638 g/in, 639 g/in, 640 g/in, 641 g/in, 642 g/in, 643 g/in, 644 g/in, 645 g/in, 646 g/in, 647 g/in, 648 g/in, 649 g/in, 650 g/in, 651 g/in, 652 g/in, 653 g/in, 654 g/in, 655 g/in, 656 g/in, 657 g/in, 658 g/in, 659 g/in, 660 g/in, 661 g/in, 662 g/in, 663 g/in, 664 g/in, 665 g/in, 666 g/in, 667 g/in, 668 g/in, 669 g/in, 670 g/in, 671 g/in, 672 g/in, 673 g/in, 674 g/in, 675 g/in, 676 g/in, 677 g/in, 678 g/in, 679 g/in, 680 g/in, 681 g/in, 682 g/in, 683 g/in, 684 g/in, 685 g/in, 686 g/in, 687 g/in, 688 g/in, 689 g/in, 690 g/in, 691 g/in, 692 g/in, 693 g/in, 694 g/in, 695 g/in, 696 g/in, 697 g/in, 698 g/in, 699 g/in, 700 g/in, 701 g/in, 702 g/in, 703 g/in, 704 g/in, 705 g/in, 706 g/in, 707 g/in, 708 g/in, 709 g/in, 710 g/in, 711 g/in, 712 g/in, 713 g/in, 714 g/in, 715 g/in, 716 g/in, 717 g/in, 718 g/in, 719 g/in, 720 g/in, 721 g/in, 722 g/in, 723 g/in, 724 g/in, 725 g/in, 726 g/in, 727 g/in, 728 g/in, 729 g/in, 730 g/in, 731 g/in, 732 g/in, 733 g/in, 734 g/in, 735 g/in, 736 g/in, 737 g/in, 738 g/in, 739 g/in, 740 g/in, 741 g/in, 742 g/in, 743 g/in, 744 g/in, 745 g/in, 746 g/in, 747 g/in, 748 g/in, 749 g/in, 750 g/in, 751 g/in, 752 g/in, 753 g/in, 754 g/in, 755 g/in, 756 g/in, 757 g/in, 758 g/in, 759 g/in, 760 g/in, 761 g/in, 762 g/in, 763 g/in, 764 g/in, 765 g/in, 766 g/in, 767 g/in, 768 g/in, 769 g/in, 770 g/in, 771 g/in, 772 g/in, 773 g/in, 774 g/in, 775 g/in, 776 g/in, 777 g/in, 778 g/in, 779 g/in, 780 g/in, 781 g/in, 782 g/in, 783 g/in, 784 g/in, 785 g/in, 786 g/in, 787 g/in, 788 g/in, 789 g/in, 790 g/in, 791 g/in, 792 g/in, 793 g/in, 794 g/in, 795 g/in, 796 g/in, 797 g/in, 798 g/in, 799 g/in, 800 g/in, 801 g/in, 802 g/in, 803 g/in, 804 g/in, 805 g/in, 806 g/in, 807 g/in, 808 g/in, 809 g/in, 810 g/in, 811 g/in, 812 g/in, 813 g/in, 814 g/in, 815 g/in, 816 g/in, 817 g/in, 818 g/in, 819 g/in, 820 g/in, 821 g/in, 822 g/in, 823 g/in, 824 g/in, 825 g/in, 826 g/in, 827 g/in, 828 g/in, 829 g/in, 830 g/in, 831 g/in, 832 g/in, 833 g/in, 834 g/in, 835 g/in, 836 g/in, 837 g/in, 838 g/in, 839 g/in, 840 g/in, 841 g/in, 842 g/in, 843 g/in, 844 g/in, 845 g/in, 846 g/in, 847 g/in, 848 g/in, 849 g/in, 850 g/in, 851 g/in, 852 g/in, 853 g/in, 854 g/in, 855 g/in, 856 g/in, 857 g/in, 858 g/in, 859 g/in, 860 g/in, 861 g/in, 862 g/in, 863 g/in, 864 g/in, 865 g/in, 866 g/in, 867 g/in, 868 g/in, 869 g/in, 870 g/in, or 871 g/in.
It is also within the scope of the present disclosure for the tensile strength at peak machine direction of the multi-layer film 2 to fall within one of many different ranges. In a first set of ranges, the tensile strength at peak machine direction for a multi-layer film having a basis weight of less than about 14 gsm—in some embodiments, less than about 13 gsm, 12 gsm, 11 gsm, or 10 gsm—is in one of the following ranges: about 575 g/in to 1,000 g/in, 575 g/in to 995 g/in, 575 g/in to 990 g/in, 575 g/in to 985 g/in, 575 g/in to 980 g/in, 575 g/in to 975 g/in, 575 g/in to 970 g/in, 575 g/in to 965 g/in, 575 g/in to 960 g/in, 575 g/in to 955 g/in, 575 g/in to 950 g/in, 575 g/in to 945 g/in, 575 g/in to 940 g/in, 575 g/in to 935 g/in, 575 g/in to 930 g/in, 575 g/in to 925 g/in, 575 g/in to 920 g/in, 575 g/in to 915 g/in, 575 g/in to 910 g/in, 575 g/in to 905 g/in, 575 g/in to 900 g/in, 575 g/in to 895 g/in, 575 g/in to 890 g/in, 575 g/in to 885 g/in, 575 g/in to 880 g/in, 575 g/in to 875 g/in, and 575 g/in to 870 g/in. In a second set of ranges, the tensile strength at peak machine direction for a multi-layer film 2 having a basis weight of less than about 14 gsm—in some embodiments, less than about 13 gsm, 12 gsm, 11 gsm, or 10 gsm—is in one of the following ranges: about 576 g/in to 1000 g/in, 577 g/in to 1000 g/in, 578 g/in to 1000 g/in, 579 g/in to 1000 g/in, 580 g/in to 1000 g/in, 581 g/in to 1000 g/in, 582 g/in to 1000 g/in, 583 g/in to 1000 g/in, 584 g/in to 1000 g/in, 585 g/in to 1000 g/in, 586 g/in to 1000 g/in, 587 g/in to 1000 g/in, 588 g/in to 1000 g/in, 589 g/in to 1000 g/in, 600 g/in to 1000 g/in, 601 g/in to 1000 g/in, 602 g/in to 1000 g/in, 603 g/in to 1000 g/in, 604 g/in to 1000 g/in, 605 g/in to 1000 g/in, 606 g/in to 1000 g/in, 607 g/in to 1000 g/in, 608 g/in to 1000 g/in, 609 g/in to 1000 g/in, 610 g/in to 1000 g/in, 611 g/in to 1000 g/in, 612 g/in to 1000 g/in, 613 g/in to 1000 g/in, 614 g/in to 1000 g/in, 615 g/in to 1000 g/in, 616 g/in to 1000 g/in, 617 g/in to 1000 g/in, 618 g/in to 1000 g/in, 619 g/in to 1000 g/in, 620 g/in to 1000 g/in, 621 g/in to 1000 g/in, 622 g/in to 1000 g/in, 623 g/in to 1000 g/in, 624 g/in to 1000 g/in, 625 g/in to 1000 g/in, 626 g/in to 1000 g/in, 627 g/in to 1000 g/in, 628 g/in to 1000 g/in, 629 g/in to 1000 g/in, 630 g/in to 1000 g/in, 631 g/in to 1000 g/in, 632 g/in to 1000 g/in, 633 g/in to 1000 g/in, 634 g/in to 1000 g/in, 635 g/in to 1000 g/in, 636 g/in to 1000 g/in, 637 g/in to 1000 g/in, 638 g/in to 1000 g/in, 639 g/in to 1000 g/in, 640 g/in to 1000 g/in, 641 g/in to 1000 g/in, 642 g/in to 1000 g/in, 643 g/in to 1000 g/in, 644 g/in to 1000 g/in, 645 g/in to 1000 g/in, 646 g/in to 1000 g/in, 647 g/in to 1000 g/in, 648 g/in to 1000 g/in, 649 g/in to 1000 g/in, 650 g/in to 1000 g/in, 651 g/in to 1000 g/in, 652 g/in to 1000 g/in, 653 g/in to 1000 g/in, 654 g/in to 1000 g/in, 655 g/in to 1000 g/in, 656 g/in to 1000 g/in, 657 g/in to 1000 g/in, 658 g/in to 1000 g/in, 659 g/in to 1000 g/in, 660 g/in to 1000 g/in, 661 g/in to 1000 g/in, 662 g/in to 1000 g/in, 663 g/in to 1000 g/in, 664 g/in to 1000 g/in, 665 g/in to 1000 g/in, 666 g/in to 1000 g/in, 667 g/in to 1000 g/in, 668 g/in to 1000 g/in, 669 g/in to 1000 g/in, 670 g/in to 1000 g/in, 671 g/in to 1000 g/in, 672 g/in to 1000 g/in, 673 g/in to 1000 g/in, 674 g/in to 1000 g/in, 675 g/in to 1000 g/in, 676 g/in to 1000 g/in, 677 g/in to 1000 g/in, 678 g/in to 1000 g/in, 679 g/in to 1000 g/in, 680 g/in to 1000 g/in, 681 g/in to 1000 g/in, 682 g/in to 1000 g/in, 683 g/in to 1000 g/in, 684 g/in to 1000 g/in, 685 g/in to 1000 g/in, 686 g/in to 1000 g/in, 687 g/in to 1000 g/in, 688 g/in to 1000 g/in, 689 g/in to 1000 g/in, 690 g/in to 1000 g/in, 691 g/in to 1000 g/in, 692 g/in to 1000 g/in, 693 g/in to 1000 g/in, 694 g/in to 1000 g/in, 695 g/in to 1000 g/in, 696 g/in to 1000 g/in, 697 g/in to 1000 g/in, 698 g/in to 1000 g/in, 699 g/in to 1000 g/in, 700 g/in to 1000 g/in, 701 g/in to 1000 g/in, 702 g/in to 1000 g/in, 703 g/in to 1000 g/in, 704 g/in to 1000 g/in, 705 g/in to 1000 g/in, 706 g/in to 1000 g/in, 707 g/in to 1000 g/in, 708 g/in to 1000 g/in, 709 g/in to 1000 g/in, 710 g/in to 1000 g/in, 711 g/in to 1000 g/in, 712 g/in to 1000 g/in, 713 g/in to 1000 g/in, 714 g/in to 1000 g/in, 715 g/in to 1000 g/in, 716 g/in to 1000 g/in, 717 g/in to 1000 g/in, 718 g/in to 1000 g/in, 719 g/in to 1000 g/in, 720 g/in to 1000 g/in, 721 g/in to 1000 g/in, 722 g/in to 1000 g/in, 723 g/in to 1000 g/in, 724 g/in to 1000 g/in, 725 g/in to 1000 g/in, 726 g/in to 1000 g/in, 727 g/in to 1000 g/in, 728 g/in to 1000 g/in, 729 g/in to 1000 g/in, 730 g/in to 1000 g/in, 731 g/in to 1000 g/in, 732 g/in to 1000 g/in, 733 g/in to 1000 g/in, 734 g/in to 1000 g/in, 735 g/in to 1000 g/in, 736 g/in to 1000 g/in, 737 g/in to 1000 g/in, 738 g/in to 1000 g/in, 739 g/in to 1000 g/in, 740 g/in to 1000 g/in, 741 g/in to 1000 g/in, 742 g/in to 1000 g/in, 743 g/in to 1000 g/in, 744 g/in to 1000 g/in, 745 g/in to 1000 g/in, 746 g/in to 1000 g/in, 747 g/in to 1000 g/in, 748 g/in to 1000 g/in, 749 g/in to 1000 g/in, 750 g/in to 1000 g/in, 751 g/in to 1000 g/in, 752 g/in to 1000 g/in, 753 g/in to 1000 g/in, 754 g/in to 1000 g/in, 755 g/in to 1000 g/in, 756 g/in to 1000 g/in, 757 g/in to 1000 g/in, 758 g/in to 1000 g/in, 759 g/in to 1000 g/in, 760 g/in to 1000 g/in, 761 g/in to 1000 g/in, 762 g/in to 1000 g/in, 763 g/in to 1000 g/in, 764 g/in to 1000 g/in, 765 g/in to 1000 g/in, 766 g/in to 1000 g/in, 767 g/in to 1000 g/in, 768 g/in to 1000 g/in, 769 g/in to 1000 g/in, 770 g/in to 1000 g/in, 771 g/in to 1000 g/in, 772 g/in to 1000 g/in, 773 g/in to 1000 g/in, 774 g/in to 1000 g/in, 775 g/in to 1000 g/in, 776 g/in to 1000 g/in, 777 g/in to 1000 g/in, 778 g/in to 1000 g/in, 779 g/in to 1000 g/in, 780 g/in to 1000 g/in, 781 g/in to 1000 g/in, 782 g/in to 1000 g/in, 783 g/in to 1000 g/in, 784 g/in to 1000 g/in, 785 g/in to 1000 g/in, 786 g/in to 1000 g/in, 787 g/in to 1000 g/in, 788 g/in to 1000 g/in, 789 g/in to 1000 g/in, 790 g/in to 1000 g/in, 791 g/in to 1000 g/in, 792 g/in to 1000 g/in, 793 g/in to 1000 g/in, 794 g/in to 1000 g/in, 795 g/in to 1000 g/in, 796 g/in to 1000 g/in, 797 g/in to 1000 g/in, 798 g/in to 1000 g/in, 799 g/in to 1000 g/in, and 800 g/in to 1000 g/in. In a third set of ranges, the tensile strength at peak machine direction for a multi-layer film 2 having a basis weight of less than about 14 gsm—in some embodiments, less than about 13 gsm, 12 gsm, 11 gsm, or 10 gsm—is in one of the following ranges: about 575 g/in to 950 g/in, 580 g/in to 945 g/in, 585 g/in to 940 g/in, 590 g/in to 935 g/in, 595 g/in to 930 g/in, 600 g/in to 925 g/in, 605 g/in to 920 g/in, 610 g/in to 915 g/in, 615 g/in to 910 g/in, 620 g/in to 905 g/in, 625 g/in to 900 g/in, 630 g/in to 900 g/in, 635 g/in to 900 g/in, 640 g/in to 900 g/in, 645 g/in to 900 g/in, 650 g/in to 900 g/in, 655 g/in to 900 g/in, 660 g/in to 900 g/in, 665 g/in to 900 g/in, 670 g/in to 900 g/in, 675 g/in to 900 g/in, 680 g/in to 900 g/in, 685 g/in to 900 g/in, 690 g/in to 900 g/in, 695 g/in to 900 g/in, 700 g/in to 900 g/in, 705 g/in to 900 g/in, 710 g/in to 900 g/in, 715 g/in to 900 g/in, 720 g/in to 900 g/in, 725 g/in to 900 g/in, 730 g/in to 900 g/in, 735 g/in to 900 g/in, 740 g/in to 900 g/in, 745 g/in to 900 g/in, 750 g/in to 900 g/in, 755 g/in to 900 g/in, 760 g/in to 900 g/in, 765 g/in to 900 g/in, 770 g/in to 900 g/in, 775 g/in to 900 g/in, 780 g/in to 900 g/in, 785 g/in to 900 g/in, 790 g/in to 900 g/in, 795 g/in to 900 g/in, and 800 g/in to 900 g/in.
In illustrative embodiments, a multi-layer film 2 in accordance with the present disclosure exhibits greater increased tensile strength at 5% strain machine direction than conventional multi-layer films of similar basis weight. The basis weight of a multi-layer film 2 in accordance with the present disclosure may be varied based on a desired tensile strength at 5% strain machine direction. In one example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a tensile strength at 5% strain machine direction of at least about 170 grams/inch (g/in). In another example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a tensile strength at 5% strain machine direction of at least about 180 grams/inch. In a further example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a tensile strength at 5% strain machine direction of at least about 190 g/in. In a further example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a tensile strength at 5% strain machine direction of at least about 200 g/in.
The tensile strength at 5% strain machine direction of a multi-layer film 2 in accordance with the present disclosure may be one of several different values or fall within one of several different ranges. For example, for a multi-layer film having a basis weight of less than about 14 gsm—in some embodiments, less than about 13 gsm, 12 gsm, 11 gsm, or 10 gsm—it is within the scope of the present disclosure to select a tensile strength at 5% strain machine direction to be greater than or equal to one of the following values: about 100 g/in, 101 g/in, 102 g/in, 103 g/in, 104 g/in, 105 g/in, 106 g/in, 107 g/in, 108 g/in, 109 g/in, 110 g/in, 111 g/in, 112 g/in, 113 g/in, 114 g/in, 115 g/in, 116 g/in, 117 g/in, 118 g/in, 119 g/in, 120 g/in, 121 g/in, 122 g/in, 123 g/in, 124 g/in, 125 g/in, 126 g/in, 127 g/in, 128 g/in, 129 g/in, 130 g/in, 131 g/in, 132 g/in, 133 g/in, 134 g/in, 135 g/in, 136 g/in, 137 g/in, 138 g/in, 139 g/in, 140 g/in, 141 g/in, 142 g/in, 143 g/in, 144 g/in, 145 g/in, 146 g/in, 147 g/in, 148 g/in, 149 g/in, 150 g/in, 151 g/in, 152 g/in, 153 g/in, 154 g/in, 155 g/in, 156 g/in, 157 g/in, 158 g/in, 159 g/in, 160 g/in, 161 g/in, 162 g/in, 163 g/in, 164 g/in, 165 g/in, 166 g/in, 167 g/in, 168 g/in, 169 g/in, 170 g/in, 171 g/in, 172 g/in, 173 g/in, 174 g/in, 175 g/in, 176 g/in, 177 g/in, 178 g/in, 179 g/in, 180 g/in, 181 g/in, 182 g/in, 183 g/in, 184 g/in, 185 g/in, 186 g/in, 187 g/in, 188 g/in, 189 g/in, 190 g/in, 191 g/in, 192 g/in, 193 g/in, 194 g/in, 195 g/in, 196 g/in, 197 g/in, 198 g/in, 199 g/in, 200 g/in, 201 g/in, 202 g/in, 203 g/in, 204 g/in, 205 g/in, 206 g/in, 207 g/in, 208 g/in, 209 g/in, 210 g/in, 211 g/in, 212 g/in, 213 g/in, 214 g/in, 215 g/in, 216 g/in, 217 g/in, 218 g/in, 219 g/in, 220 g/in, 221 g/in, 222 g/in, 223 g/in, 224 g/in, 225 g/in, 226 g/in, 227 g/in, 228 g/in, 229 g/in, 230 g/in, 231 g/in, 232 g/in, 233 g/in, 234 g/in, 235 g/in, 236 g/in, 237 g/in, 238 g/in, 239 g/in, 240 g/in, 241 g/in, 242 g/in, 243 g/in, 244 g/in, 245 g/in, 246 g/in, 247 g/in, 248 g/in, 249 g/in, 250 g/in, 251 g/in, 252 g/in, 253 g/in, 254 g/in, 255 g/in, 256 g/in, 257 g/in, 258 g/in, 259 g/in, 260 g/in, 261 g/in, 262 g/in, 263 g/in, 264 g/in, 265 g/in, 266 g/in, 267 g/in, 268 g/in, 269 g/in, 270 g/in, 271 g/in, 272 g/in, 273 g/in, 274 g/in, 275 g/in, 276 g/in, 277 g/in, 278 g/in, 279 g/in, 280 g/in, 281 g/in, 282 g/in, 283 g/in, 284 g/in, 285 g/in, 286 g/in, 287 g/in, 288 g/in, 289 g/in, 290 g/in, 291 g/in, 292 g/in, 293 g/in, 294 g/in, 295 g/in, 296 g/in, 297 g/in, 298 g/in, 299 g/in, or 300 g/in.
It is also within the scope of the present disclosure for the tensile strength at 5% strain machine direction of the multi-layer film 2 to fall within one of many different ranges. In a first set of ranges, the tensile strength at 5% strain machine direction for a multi-layer film having a basis weight of less than about 14 gsm—in some embodiments, less than about 13 gsm, 12 gsm, 11 gsm, or 10 gsm—is in one of the following ranges: about 100 g/in to 400 g/in, 100 g/in to 395 g/in, 100 g/in to 390 g/in, 100 g/in to 380 g/in, 100 g/in to 380 g/in, 100 g/in to 375 g/in, 100 g/in to 370 g/in, 100 g/in to 365 g/in, 100 g/in to 360 g/in, 100 g/in to 355 g/in, 100 g/in to 350 g/in, 100 g/in to 345 g/in, 100 g/in to 340 g/in, 100 g/in to 335 g/in, 100 g/in to 330 g/in, 100 g/in to 325 g/in, 100 g/in to 320 g/in, 100 g/in to 315 g/in, 100 g/in to 310 g/in, 100 g/in to 305 g/in, and 100 g/in to 300 g/in. In a second set of ranges, the tensile strength at 5% strain machine direction for a multi-layer film having a basis weight of less than about 14 gsm—in some embodiments, less than about 13 gsm, 12 gsm, 11 gsm, or 10 gsm—is in one of the following ranges: about 101 g/in to 400 g/in, 105 g/in to 400 g/in, 110 g/in to 400 g/in, 115 g/in to 400 g/in, 120 g/in to 400 g/in, 125 g/in to 400 g/in, 130 g/in to 400 g/in, 135 g/in to 400 g/in, 140 g/in to 400 g/in, 145 g/in to 400 g/in, 150 g/in to 400 g/in, 155 g/in to 400 g/in, 160 g/in to 400 g/in, 165 g/in to 400 g/in, 170 g/in to 400 g/in, 175 g/in to 400 g/in, 180 g/in to 400 g/in, 185 g/in to 400 g/in, 190 g/in to 400 g/in, 195 g/in to 400 g/in, 200 g/in to 400 g/in, 205 g/in to 400 g/in, 210 g/in to 400 g/in, 215 g/in to 400 g/in, 220 g/in to 400 g/in, 225 g/in to 400 g/in, 230 g/in to 400 g/in, 235 g/in to 400 g/in, 240 g/in to 400 g/in, 245 g/in to 400 g/in, 250 g/in to 400 g/in, 255 g/in to 400 g/in, 260 g/in to 400 g/in, 265 g/in to 400 g/in, 270 g/in to 400 g/in, 275 g/in to 400 g/in, and 280 g/in to 400 g/in. In a third set of ranges, the tensile strength at 5% strain machine direction for a multi-layer film 2 having a basis weight of less than about 14 gsm—in some embodiments, less than about 13 gsm, 12 gsm, 11 gsm, or 10 gsm—is in one of the following ranges: about 101 g/in to 395 g/in, 105 g/in to 390 g/in, 110 g/in to 385 g/in, 115 g/in to 380 g/in, 120 g/in to 375 g/in, 125 g/in to 370 g/in, 130 g/in to 365 g/in, 135 g/in to 360 g/in, 140 g/in to 355 g/in, 145 g/in to 350 g/in, 150 g/in to 345 g/in, 155 g/in to 340 g/in, 160 g/in to 335 g/in, 165 g/in to 330 g/in, 170 g/in to 325 g/in, 175 g/in to 320 g/in, 180 g/in to 315 g/in, 185 g/in to 310 g/in, 190 g/in to 305 g/in, 195 g/in to 300 g/in, 200 g/in to 295 g/in, and 205 g/in to 290 g/in.
In illustrative embodiments, a multi-layer film 2 in accordance with the present disclosure exhibits greater increased secant modulus machine direction (1%) than conventional multi-layer films of similar basis weight. The basis weight of a multi-layer film 2 in accordance with the present disclosure may be varied based on a desired secant modulus machine direction (1%). In one example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a secant modulus machine direction (1%) of at least about 20,000 pounds/inch (psi). In another example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a secant modulus machine direction (1%) of at least about 25,000 psi. In a further example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a secant modulus machine direction (1%) of at least about 30,000 psi. In a further example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a secant modulus machine direction (1%) of at least about 35,000 psi.
The secant modulus machine direction (1%) of a multi-layer film 2 in accordance with the present disclosure may be one of several different values or fall within one of several different ranges. For example, for a multi-layer film having a basis weight of less than about 14 gsm—in some embodiments, less than about 13 gsm, 12 gsm, 11 gsm, or 10 gsm—it is within the scope of the present disclosure to select a secant modulus machine direction (1%) to be greater than or equal to one of the following values: about 30,000 psi; 30,500 psi; 31,000 psi; 31,500 psi; 32,000 psi; 32,500 psi; 33,000 psi; 33,500 psi; 34,000 psi; 34,500 psi; 35,000 psi; 35,500 psi; 36,000 psi; 36,500 psi; 37,000 psi; 37,500 psi; 38,000 psi; 38,500 psi; 39,000 psi; 39,500 psi; 40,000 psi; 40,500 psi; 41,000 psi; 41,500 psi; 42,000 psi; 42,500 psi; 43,000 psi; 43,500 psi; 44,000 psi; 44,500 psi; 45,000 psi; 45,500 psi; 46,000 psi; 46,500 psi; 47,000 psi; 47,500 psi; 48,000 psi; 48,500 psi; 49,000 psi; 49,500 psi; 50,000 psi; 50,500 psi; 51,000 psi; 51,500 psi; 52,000 psi; 52,500 psi; 53,000 psi; 53,500 psi; 54,000 psi; 54,500 psi; 55,000 psi; 55,500 psi; 56,000 psi; 56,500 psi; 57,000 psi; or 57,500 psi.
It is also within the scope of the present disclosure for the secant modulus machine direction (1%) of the multi-layer film 2 to fall within one of many different ranges. In a first set of ranges, the secant modulus machine direction (1%) for a multi-layer film having a basis weight of less than about 14 gsm—in some embodiments, less than about 13 gsm, 12 gsm, 11 gsm, or 10 gsm—is in one of the following ranges: about 35,000 psi to 65,000 psi; 35,500 psi to 65,000 psi; 40,000 psi to 65,000 psi; 40,500 psi to 65,000 psi; 41,000 psi to 65,000 psi; 41,500 psi to 65,000 psi; 42,000 psi to 65,000 psi; 42,500 psi to 65,000 psi; 43,000 psi to 65,000 psi; 43,500 psi to 65,000 psi; 44,000 psi to 65,000 psi; 44,500 psi to 65,000 psi; 45,000 psi to 65,000 psi; 45,500 psi to 65,000 psi; 46,000 psi to 65,000 psi; 46,500 psi to 65,000 psi; 47,000 psi to 65,000 psi; 47,500 psi to 65,000 psi; 48,000 psi to 65,000 psi; 48,500 psi to 65,000 psi; 49,000 psi to 65,000 psi; 49,500 psi to 65,000 psi; 50,000 psi to 65,000 psi; 50,500 psi to 65,000 psi; 51,000 psi to 65,000 psi; 51,500 psi to 65,000 psi; 52,000 psi to 65,000 psi; 52,500 psi to 65,000 psi; 53,000 psi to 65,000 psi; 53,500 psi to 65,000 psi; 54,000 psi to 65,000 psi; 54,500 psi to 65,000 psi; 55,000 psi to 65,000 psi; 55,500 psi to 65,000 psi; 56,000 psi to 65,000 psi; 56,500 psi to 65,000 psi; and 57,000 psi to 65,000 psi. In a second set of ranges, the secant modulus machine direction (1%) for a multi-layer film 2 having a basis weight of less than about 14 gsm—in some embodiments, less than about 13 gsm, 12 gsm, 11 gsm, or 10 gsm—is in one of the following ranges: about 35,000 psi to 64,999 psi; 35,000 psi to 64,500 psi; 35,000 psi to 64,000 psi; 35,000 psi to 63,500 psi; 35,000 psi to 63,000 psi; 35,000 psi to 62,500 psi; 35,000 psi to 62,000 psi; 35,000 psi to 61,500 psi; 35,000 psi to 61,000 psi; 35,000 psi to 60,500 psi; 35,000 psi to 60,000 psi; 35,000 psi to 59,500 psi; 35,000 psi to 59,000 psi; 35,000 psi to 58,500 psi; 35,000 psi to 58,000 psi; and 35,000 psi to 57,500 psi. In a third set of ranges, the secant modulus machine direction (1%) for a multi-layer film 2 having a basis weight of less than about 14 gsm—in some embodiments, less than about 13 gsm, 12 gsm, 11 gsm, or 10 gsm—is in one of the following ranges: about 35,001 psi to 64,999 psi; 35,500 psi to 64,500 psi; 34,000 psi to 64,000 psi; 34,500 psi to 63,500 psi; 35,000 psi to 63,000 psi; 35,500 psi to 62,500 psi; 36,000 psi to 62,000 psi; 36,500 psi to 61,500 psi; 37,000 psi to 61,000 psi; 37,500 psi to 60,500 psi; 38,000 psi to 60,000 psi; 38,500 psi to 59,500 psi; 39,000 psi to 59,000 psi; 39,500 psi to 58,500 psi; 40,000 psi to 58,000 psi; 40,500 psi to 58,000 psi; 41,000 psi to 58,000 psi; 41,500 psi to 58,000 psi; 42,000 psi to 58,000 psi; 42,500 psi to 58,000 psi; 43,000 psi to 58,000 psi; 43,500 psi to 58,000 psi; 44,000 psi to 58,000 psi; 44,500 psi to 58,000 psi; 45,000 psi to 58,000 psi; 45,500 psi to 58,000 psi; 46,000 psi to 58,000 psi; 46,500 psi to 58,000 psi; 47,000 psi to 58,000 psi; 47,500 psi to 58,000 psi; 48,000 psi to 58,000 psi; 48,500 psi to 58,000 psi; 49,000 psi to 58,000 psi; 49,500 psi to 58,000 psi; 50,000 psi to 58,000 psi; 50,500 psi to 58,000 psi; 51,000 psi to 58,000 psi; 51,500 psi to 58,000 psi; 52,000 psi to 58,000 psi; 52,500 psi to 58,000 psi; 53,000 psi to 58,000 psi; 53,500 psi to 58,000 psi; 54,000 psi to 58,000 psi; 54,500 psi to 58,000 psi; 55,000 psi to 58,000 psi; 55,500 psi to 58,000 psi; 56,000 psi to 58,000 psi; 56,500 psi to 58,000 psi; and 57,000 psi to 58,000 psi.
In illustrative embodiments, a multi-layer film 2 in accordance with the present disclosure exhibits a greater Dart Impact Strength than conventional microporous breathable films of similar basis weight. The basis weight of a multi-layer film 2 in accordance with the present disclosure may be varied based on a desired Dart Impact Strength. In one example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a Dart Impact Strength of at least about 35 grams. In another example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a Dart Impact Strength of at least about 40 grams. In a further example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a Dart Impact Strength of at least about 45 grams. In a still further example, a multi-layer film 2 in accordance with the present disclosure has a basis weight of less than about 14 gsm and a Dart Impact Strength of at least about 50 grams.
The Dart Impact Strength of a multi-layer film 2 in accordance with the present disclosure may be one of several different values or fall within one of several different ranges. For example, for a multi-layer film 2 having a basis weight of less than about 14 gsm—in some embodiments, less than about 13 gsm, 12 gsm, 11 gsm, or 10 gsm—it is within the scope of the present disclosure to select a Dart Impact Strength to be greater than or equal to one of the following values: about 30 grams, 31 grams, 32 grams, 33 grams, 34 grams, 35 grams, 36 grams, 37 grams, 38 grams, 39 grams, 40 grams, 41 grams, 42 grams, 43 grams, 44 grams, 45 grams, 46 grams, 47 grams, 48 grams, 49 grams, 50 grams, 51 grams, 52 grams, 53 grams, 54 grams, 55 grams, 56 grams, 57 grams, 58 grams, 59 grams, 60 grams, 61 grams, 62 grams, 63 grams, 64 grams, 65 grams, 66 grams, 67 grams, 68 grams, 69 grams, 70 grams, 71 grams, 72 grams, 73 grams, 74 grams, 75 grams, 76 grams, or 77 grams.
It is also within the scope of the present disclosure for the Dart Impact Strength of the multi-layer film 2 to fall within one of many different ranges. In a first set of ranges, the Dart Impact Strength for a multi-layer film 2 having a basis weight of less than about 14 gsm—in some embodiments, less than about 13 gsm, 12 gsm, 11 gsm, or 10 gsm—is in one of the following ranges: about 30 grams to 250 grams, 35 grams to 250 grams, 40 grams to 250 grams, 45 grams to 250 grams, 50 grams to 250 grams, 55 grams to 250 grams, 60 grams to 250 grams, 65 grams to 250 grams, 70 grams to 250 grams, and 75 grams to 250 grams. In a second set of ranges, the Dart Impact Strength for a multi-layer film 2 having a basis weight of less than about 14 gsm—in some embodiments, less than about 13 gsm, 12 gsm, 11 gsm, or 10 gsm—is in one of the following ranges: about 50 grams to 249 grams, 50 grams to 245 grams, 50 grams to 240 grams, 50 grams to 235 grams, 50 grams to 230 grams, 50 grams to 225 grams, 50 grams to 220 grams, 50 grams to 215 grams, 50 grams to 210 grams, 50 grams to 205 grams, 50 grams to 200 grams, 50 grams to 195 grams, 50 grams to 190 grams, 50 grams to 185 grams, 50 grams to 180 grams, 50 grams to 175 grams, 50 grams to 170 grams, 50 grams to 165 grams, 50 grams to 160 grams, 50 grams to 155 grams, 50 grams to 150 grams, 50 grams to 145 grams, 50 grams to 140 grams, 50 grams to 135 grams, 50 grams to 130 grams, 50 grams to 125 grams, 50 grams to 120 grams, 50 grams to 115 grams, 50 grams to 110 grams, 50 grams to 105 grams, 50 grams to 100 grams, 50 grams to 95 grams, 50 grams to 90 grams, 50 grams to 85 grams, and 50 grams to 80 grams. In a third set of ranges, the Dart Impact Strength for a multi-layer film 2 having a basis weight of less than about 14 gsm—in some embodiments, less than about 13 gsm, 12 gsm, 11 gsm, or 10 gsm—is in one of the following ranges: about 31 grams to about 150 grams, 35 grams to about 145 grams, 40 grams to about 140 grams, 45 grams to about 135 grams, 50 grams to about 130 grams, 55 grams to about 125 grams, 60 grams to about 120 grams, 65 grams to about 115 grams, 70 grams to about 110 grams, 70 grams to about 105 grams, 70 grams to about 100 grams, 70 grams to about 95 grams, 70 grams to about 90 grams, 70 grams to about 85 grams, and 70 grams to about 80 grams.
In one example, a multi-layer film in accordance with the present disclosure may be manufactured by feed block coextrusion. In another example, a multi-layer film in accordance with the present disclosure may be made by blown film (tubular) coextrusion. Methods for feed block and blown film extrusion are described in The Wiley Encyclopedia of Packaging Technology, pp. 233-238 (Aaron L. Brody et al. eds., 2nd Ed. 1997), which is incorporated herein by reference, except that in the event of any inconsistent disclosure or definition from the present specification, the disclosure or definition herein shall be deemed to prevail. Methods for film extrusion are also described in U.S. Pat. No. 6,265,055, the entire contents of which are likewise incorporated by reference herein, except that in the event of any inconsistent disclosure or definition from the present specification, the disclosure or definition herein shall be deemed to prevail.
In some embodiments, as shown in FIG. 1, the present disclosure provides a multi-layer film 2 having a single non-cavitated skin layer 13. In other embodiments, as shown in FIG. 7, the present disclosure also provides a multi-layer non-breathable film 56 having more than one non-cavitated skin layer. For example, the multi-layer non-breathable film 56 shown in FIG. 7 includes a first non-cavitated skin layer 58, a second non-cavitated skin layer 60, and at least one cavitated core layer 62 disposed between the first non-cavitated skin layer 58 and the second non-cavitated skin layer 60. The core layer 62 in FIG. 7 is analogous to the core layer 3 shown in FIG. 1, and may include a thermoplastic polymer (or combination of thermoplastic polymers) and a solid filler (or combination of solid fillers) dispersed therein. The first non-cavitated skin layer 58 and the second non-cavitated skin layer 60 may have either the same composition as the core layer 62 or a different composition than the core layer 62. In one example, as shown in FIG. 7, the first non-cavitated skin layer 58 and the second non-cavitated skin layer 60 are analogous to the non-cavitated skin layer 13 shown in FIG. 1 and may include a thermoplastic polymer (or combination of thermoplastic polymers).
In some embodiments, as shown in FIG. 8, a multi-layer film containing a a first non-cavitated skin layer 59, a second non-cavitated skin layer 61, and at least one cavitated core layer 63 disposed between the first non-cavitated skin layer 59 and the second non-cavitated skin layer 61 may be bonded to a non-woven layer 66 to form a multi-layer structure 64 that may, in some embodiments, be used as a backsheet for a diaper, incontinence brief, and/or the like, as further described below. As shown in FIG. 8, the non-woven layer 66 may be bonded to one or the other of the first non-cavitated skin layer 59 and the second non-cavitated skin layer 61. In some embodiments, the non-woven layer 66 and the non-cavitated skin layer to which it is adjacent (e.g., second non-cavitated skin layer 61 in the depiction of FIG. 8) include the same polyolefin. For example, in some embodiments, the non-woven layer 66, the second non-cavitated skin layer 61, and/or the first non-cavitated skin layer 59 include polypropylene. In some embodiments, the non-woven layer 66, the second non-cavitated skin layer 61, and/or the first non-cavitated skin layer 59 include polypropylene, and the non-woven layer 66 is bonded to the second non-cavitated skin layer 61 by an ultrasonic weld, as further described below.
In some embodiments, as shown in FIG. 9, a multi-layer non-breathable film 68 in accordance with the present disclosure contains a first non-cavitated skin layer 70, a second non-cavitated skin layer 74, a first cavitated core layer 72 disposed between the first non-cavitated skin layer 70 and the second non-cavitated skin layer 74, a second cavitated core layer 76 disposed between the first non-cavitated skin layer 70 and the second non-cavitated skin layer 74, and at least one polar polymer layer 78 disposed between the first non-cavitated skin layer 70 and the second non-cavitated skin layer 74. The polar polymer layer 78 is configured to act as an odor barrier that is substantially impermeable to odorants that are nonpolar.
The first cavitated core layer 72 and the second cavitated core layer 76 in FIG. 9 are analogous to the cavitated core layer 3 shown in FIG. 1, and may be prepared by a process analogous to one described above. The first cavitated core layer 72 may be the same as or different than the second cavitated core layer 76. For example, the first cavitated core layer 72 and the second cavitated core layer 76 may differ from each other in thickness, breathability, pore size, thermoplastic composition, and/or the like. In one example, the first cavitated core layer 72 and the second cavitated core layer 76 are the same, and each includes a polyolefin and an inorganic filler dispersed in the polyolefin.
The first non-cavitated skin layer 70 and the second non-cavitated skin layer 74 in FIG. 9 are analogous to the non-cavitated skin layer 13 shown in FIG. 1. The first non-cavitated skin layer 70 may be the same as or different than the second non-cavitated skin layer 74 (e.g., in thickness, plastic composition, and/or the like). In one example, the first non-cavitated skin layer 70 and the second non-cavitated skin layer 74 are the same, and each includes a polyolefin.
In illustrative embodiments, as shown in FIG. 9, the multi-layer film 68 has a symmetrical structure, and the at least one polar polymer layer 78 is disposed between the first non-cavitated skin layer 70 and the first cavitated core layer 72 on one side, and between the second cavitated core layer 76 and the second non-cavitated skin layer 74 on its other side. However, alternative configurations may likewise be implemented.
The polar polymer layer 78 shown in FIG. 9 provides an internal barrier layer and—unlike first cavitated core layer 72 and second cavitated core layer 76—may be unfilled or substantially unfilled (e.g., contain an amount of solid filler that does not result in the creation of micropores as a result of stretching). In illustrative embodiments, the polar polymer layer 78 is comprised of Nylon, polyester, ethylene vinyl alcohol (EVOH) or copolymers of these materials.
The polar polymer layer 78 provides an odor barrier. In one example, a tie layer (not shown) may be used to combine dissimilar layers (e.g., polar polymer layer 78 and one or both of first cavitated core layer 72 and second cavitated core layer 76). In another example, an adhesive may be blended in one or more of the adjacent dissimilar layers, thus avoiding delamination of the adjacent, chemically different layers.
The internal polar polymer layer 78 is selected from the group consisting of elastomers, polyesters, polyamides, polyetherester copolymers, polyetheramide copolymers, polyurethanes, polyurethane copolymers, poly(etherimide) ester copolymers, polyvinyl alcohols, ionomers, celluloses, nitrocelluloses, and/or the like, and combinations thereof. In some embodiments, the at least one polar polymer layer 78 further includes an adhesive which, in some embodiments, includes polyethylene/acrylate copolymer, ethylene/methyl acrylate copolymer, acid-modified acrylate, anhydride-modified acrylate, ethylene vinyl acetate, acid/acrylate-modified ethylene vinyl acetate, anhydride-modified ethylene vinyl acetate, and/or the like, or a combination thereof. In one example, the internal polar polymer layer 78 may constitute from about 0.5% to about 30% of the total thickness of the film 68. In another example, the polar polymer layer 78 may constitute from about 1% to about 20% of the total thickness of the film 68. In a further example, the polar polymer layer 78 may constitute from about 2% to about 10% of the total thickness of the film 68. In some embodiments (not shown), the multi-layer film 68 includes a plurality of polar polymer layers 78, and the above-described exemplary ranges of thickness percentages may be applied to the sum of the multiple polar polymer layers within the film. Multi-layer non-breathable films 68 in accordance with the present disclosure may include one or more internal polar polymer layers 78, which may be contiguous with each other or with interposed microporous breathable layers such as first cavitated core layer 72 and second cavitated core layer 76. In illustrative embodiments, one or more polar polymer layers 78 provided in a multi-layer breathable barrier film 68 in accordance with the present disclosure are monolithic and do not contain any fillers that provide sites for the development of micropores. However, polar polymer layers may contain other additives to confer desired properties to the polar polymer layer.
Representative materials for the polar polymer layer 78 include but are not limited to hygroscopic polymers such as ε-caprolactone (available from Solvay Caprolactones), polyether block amides (available from Arkema PEBAX), polyester elastomer (such as Dupont Hytrel or DSM Arnitel) and other polyesters, polyamides, celluloses (e.g., cellulose fibers), nitrocelluloses (e.g., nitrocellulose fibers), ionomers (e.g., ethylene ionomers), and/or the like, and combinations thereof. In one example, fatty acid salt-modified ionomers as described in the article entitled “Development of New Ionomers with Novel Gas Permeation Properties” (Journal of Plastic Film and Sheeting, 2007, 23, No. 2, 119-132) may be used as a polar polymer layer 78. In some embodiments, sodium, magnesium, and/or potassium fatty acid salt-modified ionomers may be used to provide desirable water vapor transmission properties. In some embodiments, the polar polymer layer 78 is selected from the group consisting of hygroscopic elastomers, polyesters, polyamides, polyetherester copolymers (e.g., a block polyetherester copolymer), polyetheramide copolymers (e.g., a block polyetheramide copolymer), polyurethanes, polyurethane copolymers, poly(etherimide) ester copolymers, polyvinyl alcohols, ionomers, celluloses, nitrocelluloses, and/or the like, and combinations thereof. In one example, copolyether ester block copolymers are segmented elastomers having soft polyether segments and hard polyester segments, as described in U.S. Pat. No. 4,739,012. Representative copolyether ester block copolymers are sold by DuPont under the trade name HYTREL®. Representative copolyether amide polymers are copolyamides sold under the trade name PEBAX® by Atochem Inc. of Glen Rock, N.J. Representative polyurethanes are thermoplastic urethanes sold under the trade name ESTANE® by the B. F. Goodrich Company of Cleveland, Ohio. Representative copoly(etherimide) esters are described in U.S. Pat. No. 4,868,062.
In some embodiments, the polar polymer layer 78 may include or be blended with a thermoplastic resin. Representative thermoplastic resins that may be used for this purpose include but are not limited to polyolefins, polyesters, polyetheresters, polyamides, polyether amides, urethanes, and/or the like, and combinations thereof. In some embodiments, the thermoplastic polymer may include (a) a polyolefin, such as polyethylene, polypropylene, poly(i-butene), poly(2-butene), poly(i-pentene), poly(2-pentene), poly(3-methyl-1-pentene), poly(4-methyl-1-pentene), 1,2-poly-1,3-butadiene, 1,4-poly-1,3-butadiene, polyisoprene, polychloroprene, polyacrylonitrile, polyvinyl acetate, poly(vinylidene chloride), polystyrene, and/or the like, and combinations thereof; (b) a polyester such as poly(ethylene terephthalate), poly(butylenes)terephthalate, poly(tetramethylene terephthalate), poly(cyclohexylene-1,4-dimethylene terephthalate), poly(oxymethylene-1,4-cyclohexylenemethyleneoxyterephthaloyl), and/or the like, and combinations thereof; and (c) a polyetherester, such as poly(oxyethylene)-poly(butylene terephthalate), poly(oxytetramethylene)-poly(ethylene terephthalate), and/or the like, and combinations thereof; and/or (d) a polyamide, such as poly(6-aminocaproic acid), poly(,-caprolactam), poly(hexamethylene adipamide), poly(hexamethylene sebacamide), poly(1 1-aminoundecanoic acid), and/or the like, and combinations thereof.
In illustrative embodiments the hygroscopic polymer is a hygroscopic elastomer. A variety of additives may be added to the polar polymer layer 78 to provide additional properties such as antimicrobial effects, odor control, static decay, and/or the like.
One or more of the polar polymer layer 78, the first cavitated core layer 72, and the second cavitated core layer 76 in the multi-layer non-breathable film 68 may include one or more adhesives for adhering the internal polar polymer layer 78 to contiguous layers to form at least a portion of the multi-layer film 68. In one example, adhesive may be components suitable for adhering two or more layers together. In one example, adhesives are compatibilizing adhesives that increase the compatibility of the layers as well as adhering the layers to one another. The adhesives may be included in the resin or other extrudable material before extruding that resin into the polar polymer layer 78. Representative compatibilizing adhesives include but are not limited to polyethylene/acrylate copolymer, ethylene/methyl acrylate copolymer, acid-modified acrylate, anhydride-modified acrylate, ethylene vinyl acetate, acid/acrylate-modified ethylene vinyl acetate, anhydride-modified ethylene vinyl acetate, and/or the like, and combinations thereof. In one example, when one of the first cavitated core layer 72, the second cavitated core layer 76, and the polar polymer layer 78 includes an adhesive, the adhesive may have a relatively high methacrylate content (e.g., a methacrylate content of at least about 20% to 25%). In some embodiments, the internal polar polymer layer 78 may be prepared from blends including up to about 50% by weight adhesive and at least about 50% by weight hygroscopic polymer.
In some embodiments, the hygroscopic polymer may be dried before it is extruded. Feeding pre-dried hygroscopic elastomer in small amounts to an extruder has proven to be effective in avoiding moisture absorption, preventing hydrolysis of the hygroscopic elastomer, and reducing or eliminating the formation of dark blue gels and holes in web. In some higher stretch ratio cases, gels rendered holes and even web break.
A multi-layer non-breathable barrier film 68 in accordance with the present disclosure may contain one or a plurality of polar polymer layers 78, each of which may be placed in any order in the inner layers of the film structure. In illustrative embodiments, the polar polymer layer 78 is not placed on the outer surface of the resultant film 68 in order to avoid damage caused by foreign materials. In one example, when the film 68 contains a plurality of polar polymer layers 78, individual polar polymer layers 78 are not placed adjacent to each other inside the film in order to increase efficacy. When a plurality of polar polymer layers 78 is used, the individual polar polymer layers 78 may differ from each other in thickness and/or type of thermoplastic polymer.
In one example, as shown in FIG. 9, a representative structure for a multi-layer breathable barrier film 68 contains five layers with one polar polymer layer 78 being in the center of the structure and two microporous, breathable cavitated core layers (72 and 74, respectively) being arranged symmetrically around the central polar polymer layer 78. In one example, the five-layer breathable barrier film has a A1-C1-B-C2-A2 structure as shown in FIG. 9, wherein: A1 represents a first non-cavitated skin layer; C1 represents a first microporous, breathable cavitated core layer; B represents a polar polymer layer; C2 represents a second microporous breathable cavitated core layer, which may be the same as or different than the first microporous breathable cavitated core layer C1; and A2 represents a second non-cavitated skin layer, which may be the same as or different than the first non-cavitated skin layer A1.
In one example, the first cavitated core layer 72 and/or the second cavitated core layer 76 (C1 and/or C2) contains polyethylene (e.g., metallocene polyethylene resin and/or low density polyethylene resin) and calcium carbonate. Additional adhesives, antioxidants, colorants, and/or processing aids may optionally be added. The microporous breathable cavitated core layer C1 may differ from the microporous breathable film cavitated core layer C2 in the amount and/or identity of solid filler present (e.g., calcium carbonate, barium sulfate, talc, glass spheres, other inorganic particles, etc.). The inner polar polymer layer B may contain a hygroscopic elastomer such as Dupont HYTREL PET and an adhesive such as Dupont BYNEL 3101 20% EVA or Dupont AC1820 acrylate, with additional antioxidants, colorants, and processing aids optionally being added. In one example, the inner polar polymer layer B contains adhesive and about 50% by weight or more of hygroscopic elastomer. Instead of a polyester elastomer, other hygroscopic polymers, such as ε-caprolactone, polyester block amides, polyester elastomers, polyamides, and blends thereof may be utilized as the inner polar polymer layer.
Multi-layer non-breathable films 68 of a type described above are not limited to any specific kind of film structure. Other film structures may likewise achieve the same or a similar result as the three-layer film 56 shown in FIG. 7 or the five-layer structure A-C-B-C-A shown in FIG. 9. Film structure is a function of equipment design and capability. For example, the number of layers in a film depends only on the technology available and the desired end use for the film. Representative examples of film structures that may be implemented in accordance with the present disclosure include but are not limited to the following, wherein A represents a non-cavitated skin layer (e.g., 13, 58, 60, 59, 61, 70, and/or 74) and C represents a microporous, breathable cavitated core layer (e.g., 3, 62, 63, 72, 76, and/or 82):
A-C-A
A-A-C-A
A-C-A-A
A-A-C-A-A
A-C-A-A-A
A-C-A-C-A
A-C-A-A-A-A-A
A-A-C-A-A-A-A
A-A-A-C-A-A-A
A-C-A-A-A-C-A
A-C-A-A-C-A-A
A-C-A-C-A-A-A
A-C-A-C-A-C-A
A-C-A-A-A-A-A-A
A-A-C-A-A-A-A-A
A-A-A-C-A-A-A-A
A-C-A-A-A-A-C-A.
In the above-described exemplary film structures, each of the microporous breathable cavitated core layers C may include two or more microporous breathable film layers in order to better control other film properties, such as the ability to bond to nonwovens. In addition, when the film structure further includes a polar polymer layer B (e.g., 78), some exemplary film structures include but are not limited to the following:
A-C-B-C-A
A-C-A-C-B-C-A
A-C-B-C-A-C-A
A-C-A-C-B-C-A-C-A
A-C-B-C-A-C-A-C-A
A-C-B-C-A-B-C-A
Additionally, die technology that allows production of multiple layers in a multiplier fashion may be used. For example, an ABA structure may be multiplied from about 10 to about 1000 times. The resulting 10-time multiplied ABA structure may be expressed as follows:
A-B-A-A-B-A-A-B-A-A-B-A-A-B-A-A-B-A-A-B-A-A-B-A-A-B-A-A-B-A
In some embodiments described above, the compositions used to extrude cavitated core layers (e.g., 3, 62, 63, 72, 76, and/or 82) contain a solid filler. Thus, upon stretching, the cavitated core layers becomes microporous and breathable. By contrast, non-cavitated skin layers (e.g., 13, 58, 60, 59, 61, 70, and/or 74) are generally not breathable since they do not contain a solid filler prior to stretching. However, in some embodiments, the thickness and composition of one or more skin layers of a multi-layer film in accordance with the present disclosure may be selected so that when the precursor film is subsequently stretched, the resulting film is breathable. In one example, a pair of skin layers sandwiching a core layer may be relatively thin and together account for no more than about 30% of the total film thickness. Thus, in some embodiments, regardless of whether or not a skin layer contains a solid filler, the skin layer may still be breathable. For example, the skin layer may include one or more discontinuities that are introduced during the stretching process. The likelihood of discontinuities forming in a skin layer may increase as the thickness of the skin layer subjected to stretching decreases.
In some embodiments, as shown in FIG. 10, a multi-layer partially-breathable film 80 may be provided. As shown in FIG. 10, the multi-layer partially-breathable film 80 contains at least one cavitated core layer 82 and at least one skin layer 84. The cavitated core layer 82 contains one or a plurality of polyolefins and one or a plurality of inorganic fillers. The skin layer 84 includes one or a plurality of polyolefins, which may be the same as or different than the polyolefins of the cavitated core layer 82, and further includes one or a plurality of discontinuities 86. Due to the discontinuity 86 present in skin layer 84, the multi-layer partially-breathable film 80 has a microporous breathable region 88 and a non-microporous, non-breathable region 90.
The multi-layer partially-breathable film 80 may be formed, for example, by applying a surface modification technique, including but not limited to corona treatment, to the pre-stretched film. The surface modification technique may be used to treat regions of the pre-stretched film that are intended to become breathable, such that the film will be configured to break in the treated regions once it is subjected to stretching. Alternatively, a multi-layer partially-breathable film 80 may be formed by selectively applying CD-IMG stretching more aggressively to certain regions of the film (e.g., particular lanes) that are intended to become breathable. For example, portions of the quenched film that were previously subjected to selective cross-directional stretching may become breathable upon further downweb stretching in the machine direction, whereas portions of the quenched film that did not previously receive prior cross-directional stretching (or received less aggressive cross-directional stretching) may be configured to remain non-breathable even after being subjected to downweb machine direction stretching.
Representative applications using a multi-layer film (e.g., 2), a multi-layer non-breathable film (e.g., 56, 64, and/or 68) and/or a multi-layer partially-breathable film (e.g., 80) include but are not limited to medical gowns, diaper back sheets, drapes, packaging, garments, articles, carpet backing, upholstery backing, bandages, protective apparel, feminine hygiene, building construction, bedding and/or the like. Films in accordance with the present disclosure may be laminated to a fabric, scrim, or other film support by thermal, ultrasonic, and/or adhesive bonding. The support may be attached to at least one face of the film and or to both faces of the film. The laminate may be made using wovens, knits, nonwovens, paper, netting, or other films. Adhesive bonding may be used to prepare such laminates. Adhesive bonding may be performed with adhesive agents such as powders, adhesive webs, liquid, hot-melt and solvent-based adhesives. Additionally, these types of support may be used with ultrasonic or thermal bonding if the polymers in the support are compatible with the film surface. Laminates of the present multilayer films and nonwoven fabrics may provide surgical barriers. In one example, the fabrics are spunbonded or spunbond-meltblown-spunbond (SMS) fabrics. In another example, the fabrics may be spunlaced, airlaid, powder-bonded, thermal-bonded, or resin-bonded. The encasing of the polar polymer layer 78 protects the polar polymer layer 78 from mechanical damage or thermal damage and allows for thermal and ultrasonic bonding of the multilayer film at extremely low thicknesses.
Multi-layer non-breathable or partially breathable films in accordance with the present disclosure may be used for applications such as personal hygiene products. In illustrative embodiments, a personal hygiene product in accordance with the present disclosure includes at least one inner multi-layer film (e.g., 2, 56, 64, 68, and/or 80) prepared by a process as described above and at least one outer non-woven layer. At least one non-cavitated skin layer of a multi-layer film in accordance with the present disclosure is configured for attachment to and/or bonding with the outer non-woven layer. In some embodiments, the personal hygiene product further includes at least one polar polymer layer 78 disposed between a pair of non-cavitated skin layers, as shown in FIG. 9.
In one example, the at least one non-cavitated skin layer of a multi-layer film in accordance with the present disclosure is bonded to the at least one outer non-woven layer without an adhesive (e.g., via heat sealing, ultrasonic welding, and/or the like). In some embodiments, each of the at least one non-cavitated skin layer and the at least one outer non-woven layer includes polypropylene and/or polyethylene. In illustrative embodiments, each of the at least one non-cavitated skin layer and the at least one outer non-woven layer includes polypropylene.
In illustrative embodiments, the personal hygiene product in accordance with the present disclosure is configured as an incontinence brief, a diaper, a surgical gown, or a feminine hygiene product.
In some embodiments, as further explained below, a multi-layer film in accordance with the present disclosure may be used as an ultrathin backsheet (e.g., for a diaper). Functions of a diaper backsheet may include one or more of the following: (a) provide a barrier to liquid and solid waste (e.g., through the use of absorbent cores, which typically contain superabsorbent polymers); (b) provide a barrier to odor; (c) provide opacity to mask soiling (e.g., by loading a polymeric layer of the diaper backsheet with TiO2); and (d) be able to carry print and/or artwork. With regard to (a), superabsorbent polymers (SAPs) are typically sharp-cornered particles with a tendency to rupture backsheets under compressive pressure or when dragged at a different speed from the barrier film. With regard to (c), the challenge increases with decreasing film thickness since the proportion of TiO2 in the blend grows higher with any thickness decrease, and the TiO2 adds cost and detracts from desired properties.
Heretofore, diaper backsheets have typically been embossed in order to better simulate a cloth-like appearance. However, virtually all diaper backsheets nowadays are covered with a non-woven material, and an emboss pattern no longer serves its original purpose.
It has been discovered that a chill cast quenching process in accordance with the present teachings may be used to prepare a microporous breathable film (a.k.a. a cavitated film) that has a thickness of as low as about 0.28 mils (about 6.7 gsm) and yet exceptionally good puncture strength. Thus, in view of the fact that an embossing process is no longer required for diaper backsheets, and in further view of the fact that a chill cast quenching process of a type described herein (e.g., vacuum box, air blanket, and/or air knife) may be used to form an exceptionally thin yet durable film, an ultrathin diaper backsheet exhibiting good puncture resistance to SAP particles may be prepared by bonding a simple non-woven layer to a multi-layer non-breathable film in accordance with the present disclosure (i.e., a multi-layer non-breathable film prepared by a chill cast quenching process of a type described herein).
As noted above, diaper fouling has heretofore typically been masked by loading a polymeric layer in the diaper backsheet with expensive TiO2. Surprisingly and unexpectedly, it has been found that cavitation may serve as an alternative opacification aid to reduce or eliminate reliance on TiO2 for masking diaper fouling. The at least one cavitated core layer (e.g., 3, 62, 63, 72, 76, and/or 82) present in a multi-layer film in accordance with the present teachings may thus be used to provide a low-cost alternative to opacification.
While neither desiring to be bound by any particular theory nor intending to limit in any measure the scope of the appended claims or their equivalents, it is presently believed that the cavitations induced by a solid filler (e.g., CaCO3) when a film is activated serve to diffuse light at a lower cost than expensive TiO2 particles. Although cavitation would likewise occur in a microporous breathable film prepared by a chill cast process in accordance with the present disclosure, microporosity/breathability is not required in the case of a diaper backsheet. Accordingly, the breathability aspect of a microporous breathable layer (e.g., a cavitated core layer) may be turned off or otherwise reduced (e.g., by attaching the cavitated core layer to at least one non-cavitated skin layer).
In illustrative embodiments, an ultrathin backsheet in accordance with the present disclosure may resemble the multi-layer non-breathable film 56 shown in FIG. 7. When bonded to a non-woven material, an ultrathin backsheet in accordance with the present disclosure may resemble the multi-layer structure 64 shown in FIG. 8. Since non-woven materials such as the non-woven layer 66 in FIG. 8 are typically polypropylene-based, the first non-cavitated skin layer 58 and the second non-cavitated skin layer 60 shown in FIG. 7 (also, the first non-cavitated skin layer 59 and the second non-cavitated skin layer 66 shown in FIG. 8) may likewise be polypropylene-based in order to be ultrasonically compatible with the nonwoven layer 66 and to be more thermally resistant to adhesive temperatures (a consideration that becomes increasingly important as film thicknesses decrease). A multi-layer film having non-filled non-cavitated skin layers will be more compatible with ultrasonic bonding than an analogous microporous layer that contains mineral filler at the surface or just beneath a thin non-breathable skin layer.
In addition, it has been found that a multi-layer non-breathable film 56 as shown in FIG. 7 having a polypropylene-based first non-cavitated skin layer 58 and a polypropylene-based second non-cavitated skin layer 60 feels softer to the touch and is quieter than a similar polypropylene-based film that does not contain at least one cavitated core layer 62. While neither desiring to be bound by any particular theory nor intending to limit in any measure the scope of the appended claims or their equivalents, it is presently believed that the cavitations present in the at least one cavitated core layer 62 confer the increased softness and quietness properties to multi-layer non-breathable films in accordance with the present disclosure. Both softness and quietness may be desirable attributes for applications such as diaper backsheets, incontinence briefs, and the like.
In illustrative embodiments, each of the first non-cavitated skin layer 58 and the second non-cavitated skin layer 60 shown in FIG. 7 contains polypropylene (e.g., homopolymer, impact copolymer). In some embodiments, the first non-cavitated skin layer 58 and the second non-cavitated skin layer 60 are comprised primarily of polypropylene (e.g., in some embodiments, greater than about 50 wt. %, 55 wt. %, 60 wt. %, 65 wt. %, 70 wt. %, 75 wt. %, 80 wt. %, 85 wt. %, 90 wt. %, 95 wt. %, 96 wt. %, 97 wt. %, 98 wt. %, or 99 wt. %). In other embodiments, the first non-cavitated skin layer 58 and the second non-cavitated skin layer 60 consist essentially of polypropylene. In illustrative embodiments, at least one of the first non-cavitated skin layer 58 and the second non-cavitated skin layer 60 is non-filled. In some embodiments, both of the first non-cavitated skin layer 58 and the second non-cavitated skin layer 60 are non-filled.
In illustrative embodiments, the at least one cavitated core layer 62 shown in FIG. 7 contains a polyolefin (e.g., polyethylene and/or polypropylene), CaCO3 filler and, optionally, a minimal amount of TiO2 (e.g., in order to achieve a desired opacity at minimum cost). Since breathability per se is not a desired property in this application, a lower grade of CaCO3 may be used in place of the higher grades that may be preferable when breathability is a goal in and of itself). The multi-layer film 56 in FIG. 7 may be subjected to crossweb CD-IMG orientation to cavitate the core layer 62 and then to downweb MD stretch to add tensile strength for converting.
As the thickness of a backsheet film decreases, it may also be useful to include a layer that is highly impermeable to odorants. Polar molecules (e.g., nylon, EVOH, PET) may be used as described above in relation to FIG. 9. If such polar molecules are used, there are advantages to not using them as exterior layers since the polar molecules are less compatible thermally or adhesively with the polyolefins commonly used in disposable products. Moreover, these hydrophilic polymers may create extrusion problems when present on a film exterior. Similarly, a central non-breathable layer may be selected for toughness, stiffness, or thermal resistance properties, and there may be advantages with respect to curl or other processing issues in keeping such layers internal. If structures are made with hydrophobic and hydrophilic materials, tie adhesives may be blended in or co-extruded as tie layers.
The following examples and representative procedures illustrate features in accordance with the present disclosure, and are provided solely by way of illustration. They are not intended to limit the scope of the appended claims or their equivalents.
EXAMPLES
General
For production of the example films, an extrusion cast line with up to 3 extruders was used. The “A” and “B” extruders are 2½″ in diameter, and the “C” extruder is 1¾″ in diameter. The extruders feed into a combining feedblock manufactured by Cloeren Corporation of Orange, Tex., which can layer the A, B and C extruder outputs in a variety of configurations. From the feedblock, the molten polymer proceeds into a monolayer cast die (manufactured by Cloeren) that is about 36″ wide. The die has an adjustable gap. For the samples described herein, the adjustable gap was maintained between 10 and 40 mils. The molten polymer drops down to a chill roll. For the samples described herein, the chill roll had an embossed pattern FST-250 which was engraved by Pamarco of Roselle, N.J. as their pattern P-2739. The embossed pattern P-2739 is a square pattern (e.g., with lines nearly aligned with the Machine Direction) with 250 squares per inch and a depth of about 31 microns. The roll itself has an 18″ diameter with internal water cooling. The engrave roll pattern may be replaced with other patterns that are shallow enough not to interfere with a vacuum box quench. One alternative is a 40 Ra pattern (40 micro-inch average roughness) generated by a sand-blasting process on a chrome plated roll.
Comparison of Conventional Embossed Backsheet Film to Chill Cast Vacuum Box Backsheet Film
In this experiment, a skinned multi-layer backsheet film having a structure CBBBC was prepared from the formulation XC3-828-2300.0 shown in Table 1.
TABLE 1
Composition of XC3-828-2300.0 Used to Make a
CBBBC Skinned Multi-Layer Non-Breathable Film
Amount of
Layer % Component
EXTRUDER (Total) COMPONENT (Weight %)
B 60 CF7414 (CaCO3) 70
EXCEED LL3518 30
(ExxonMobil,
metallocene polyethylene
resin, narrow MWD,
density = 0.918 g/cm3)
C 20/20 C702-20 90
(split) (Braskem, polypropylene
impact copolymer)
LGA-105 10
(ExxonMobil, low
density polyethylene
resin)
The composition of the CaCO3-containing formulation (CF7414) listed in Table 1 is specified below in Table 2.
TABLE 2
Composition of the CF7414 Formulation Shown in Table 1.
Component Amount of Component
EXCEED LL3518 28
FilmLink 500 (CaCO3) 60
TiO 2 12
The molten web formed by extrusion of the composition XC3-828-2300.0 shown in Table 1 was quenched by a chill cast vacuum box process in accordance with the present disclosure on a 250T roll (1749.9 rpm setting). For comparison, two backsheet films having a structure ABBBA were prepared from a formulation XC3-828-2204.0 using a conventional embossing process. The physical properties of an ultrathin (9.26 gsm) backsheet film obtained from the composition XC3-828-2300.0 by a chill cast vacuum box process in accordance with the present disclosure, and the physical properties of two conventional backsheet films (10.16 gsm and 7.00 gsm) obtained from the composition XC3-828-2204.0, are summarized below in Table 3
TABLE 3
Comparison of Physical Properties of Backsheet Films Prepared by Conventional
Embossing Process vs. Backsheet Film Prepared by Chill Cast Vacuum Box Process.
Comparative Examples Example (Chill Cast
(Conventional Embossing Vacuum Box Process
Process with XC3-828-2204.0 with XC3-828-2300.0
Formulation) Formulation)
Physical Property Units Comp. Ex A Comp. Ex B Ex. 1
Basis Weight g/m2 10.16 7.00 9.26
Emboss Depth mil 1.33 0.93 0.40
Light Transmission % 69.4 77.7 60.3
Gloss - % @ 45° 3.6 3.2 6.2
Gloss - In % @ 45° 3.5 3.2 5.9
COF, Static - Out Index 0.69 1.03 1.412
COF, Static - In\In Index 1.62 1.95 1.432
COF, Kinetic - Out Index 0.55 0.88 1.096
COF, Kinetic - In\In Index 1.46 1.72 1.076
Tensile Gauge MD mil 0.42 0.29 0.31
Tensile @ Peak MD grams/inch 904 630 871
Strain @ Peak MD % 492 425 242
Tensile @ Break MD grams/inch 904 630 871
Strain @ Break MD % 492 425 242
Tensile @ Yield MD grams/inch 356 357 350
Strain @ Yield MD % 20 39 10
Tensile @ 5% Strain MD grams/inch 209 136 282
Tensile @ 10% Strain MD grams/inch 289 201 354
Tensile @ 25% Strain MD grams/inch 381 288 400
Tensile @ 50% Strain MD grams/inch 481 390 412
Tensile @ 100% Strain MD grams/inch 533 423 443
Secant Modulus MD (1%) PSI 23773 22116 57,822
TEA MD FtLb/in2 2681 2494 1,485
MD Elmendorg Tear gf 20.9* 9.8* 12.7*
Tensile Gauge TD mil 0.42 0.29 0.31
Tensile @ Peak TD grams/inch 578 348 293
Strain @ Peak TD % 581 506 427
Tensile @ Break TD grams/inch 577 347 292
Strain @ Break TD % 581 505 427
Tensile @ Yield TD grams/inch 255 186 226
Strain @ Yield TD % 18 19 17
Tensile @ 5% Strain TD grams/inch 145 93 140
Tensile @ 10% Strain TD grams/inch 210 148 200
Tensile @ 25% Strain TD grams/inch 260 188 234
Tensile @ 50% Strain TD grams/inch 251 181 230
Tensile @ 100% Strain TD grams/inch 259 185 220
Secant Modulus TD (1%) PSI 19801 15243 26,463
TEA TD FtLb/in2 1768 1460 1,177
TD Elmendorf Tear gf 204 222 197
Dart Drop (26″) g 74 49 77
§ Slow Puncture - Out gf 616 422 293
The composition of formulation XC3-828-2204.0 used in Comparative Examples A and B is shown below in Table 4.
TABLE 4
Composition of XC3-828-2204.0 Used to Make Conventional
Embossed Backsheet Films in Comparative Examples A and B
Amount of
Layer % Component
EXTRUDER (Total) COMPONENT (Weight %)
B 60 EXCEED LL3527 62.5
(ExxonMobil,
metallocene polyethylene
resin, narrow MWD,
density = 0.927 g/cm3)
LGA-105 20
(ExxonMobil, low
density polyethylene
resin)
VISTAMAXX 6202 7.5
(ExxonMobil, olefinic
elastomer performance
polymer)
111017P White PE MB 10
(Ampacet, white
masterbatch LLD
polyethylene)
A 20/20 PP3155 75
(split) (ExxonMobil,
polypropylene
homopolymer)
LGA-105 25
(ExxonMobil, low
density polyethylene
resin)
Surprisingly and unexpectedly, as shown by the data in Table 3, the multi-layer non-breathable film in accordance with the present disclosure (Ex. 1) essentially matched the tensile strength at peak machine direction of a much thicker conventional embossed film (Comp. Ex. A). In addition, the multi-layer non-breathable film in accordance with the present disclosure (Ex. 1) also exhibited higher tensile strength at 5% strain machine direction and substantially higher secant modulus machine direction (1%) than the much thicker conventional embossed film (Comp. Ex. A). Furthermore, surprisingly and unexpectedly, the multi-layer non-breathable film in accordance with the present disclosure (Ex. 1) exhibited a Dart Impact Strength that was greater than that of the much thicker conventional embossed film (Comp. Ex. A).
The embossed process is prone to draw resonance. As a result, microporous breathable films prepared by a conventional embossing process typically include LDPE to assist in the processing. However, for microporous breathable films prepared by a chill cast vacuum box quenching process in accordance with the present teachings, the LDPE may be omitted, thereby affording stronger films having properties that were heretofore unachievable with conventional films.

Claims (20)

The invention claimed is:
1. A process for making a multi-layer non-breathable film, the multi-layer non-breathable film comprising a first non-cavitated skin layer, a second non-cavitated skin layer, and at least one cavitated core layer disposed between the first non-cavitated skin layer and the second non-cavitated skin layer, the process comprising the steps of
extruding two or more extrudable materials to form a molten web, wherein at least a first extrudable material comprises a first polyolefin and an inorganic filler and is configured to form the at least one cavitated core layer, and wherein at least a second extrudable material comprises a second polyolefin and is configured to form each of the first non-cavitated skin layer and the second non-cavitated skin layer,
casting the molten web against a surface of a chill roll using an air knife, air blanket, a vacuum box, or a combination thereof and without use of a nip to form a quenched film, and
stretching the quenched film to form the multi-layer film, wherein the stretching comprises cross-directional intermeshing gear (CD-IMG) stretching and machine direction (MD) stretching,
wherein the first polyolefin and the second polyolefin are the same or different,
wherein the process for making the multi-layer non-breathable film does not include machine direction intermeshing gear (MD-IMG) stretching, and wherein the MD stretching occurs after the CD-IMG stretching.
2. The process of claim 1, wherein the first polyolefin and the second polyolefin are individually selected from the group consisting of polyethylene, polypropylene, and a combination thereof.
3. The process of claim 1, wherein the first polyolefin comprises polypropylene.
4. The process of claim 1, wherein the second polyolefin comprises polypropylene.
5. The process of claim 1, wherein the each of the first polyolefin and the second polyolefin comprises polypropylene.
6. The process of claim 1, wherein an average particle size of the inorganic filler is between about 0.1 microns and about 15 microns.
7. The process of claim 1, wherein the molten web is cast against the surface of the chill roll under negative pressure by the vacuum box.
8. The process of claim 1, wherein the molten web is cast against the surface of the chill roll under positive pressure by the air knife.
9. The process of claim 1, wherein the stretching further comprises cold drawing.
10. The process of claim 1 further comprising annealing the multi-layer non-breathable film in which the annealing is performed at a temperature of between about 75 degrees Fahrenheit and about 225 degrees Fahrenheit.
11. The process of claim 1 further comprising attaching at least a portion of either the first non-cavitated skin layer or the second non-cavitated skin layer to a nonwoven material.
12. The process of claim 11, wherein the nonwoven material and at least the portion of either the first non-cavitated skin layer or the second non-cavitated skin layer attached to the nonwoven material comprises polypropylene.
13. A process for making a multi-layer non-breathable film, the multi-layer non-breathable film comprising a first non-cavitated skin layer, a second non-cavitated skin layer, at least one cavitated core layer disposed between the first non-cavitated skin layer and the second non-cavitated skin layer, and at least one polar polymer layer disposed between the first non-cavitated skin layer and the second non-cavitated skin layer, the process comprising the steps of
extruding three or more extrudable materials to form a molten web, wherein at least a first extrudable material comprises a first polyolefin and an inorganic filler and is configured to form the at least one cavitated core layer, wherein at least a second extrudable material comprises a second polyolefin and is configured to form each of the first non-cavitated skin layer and the second non-cavitated skin layer, and wherein at least a third extrudable material comprises a hygroscopic polymer and is configured to form the at least one polar polymer layer,
casting the molten web against a surface of a chill roll using an air knife, air blanket, a vacuum box, or a combination thereof and without use of a nip to form a quenched film, and
stretching the quenched film to form the multi-layer film, wherein the stretching comprises cross-directional intermeshing gear (CD-IMG) stretching and machine direction (MD) stretching,
wherein the first polyolefin and the second polyolefin are the same or different,
wherein the process for making the multi-layer non-breathable film does not include machine direction intermeshing gear (MD-IMG) stretching, and wherein the MD stretching occurs after the CD-IMG stretching.
14. The process of claim 13, wherein the hygroscopic polymer is selected from the group consisting of hygroscopic elastomers, polyesters, polyamides, polyetherester copolymers, polyetheramide copolymers, polyurethanes, polyurethane copolymers, poly(etherimide) ester copolymers, polyvinyl alcohols, ionomers, celluloses, nitrocelluloses, and a combination thereof.
15. The process of claim 13, wherein the third extrudable material further comprises an adhesive and the adhesive comprises polyethylene/acrylate copolymer, ethylene/methyl acrylate copolymer, acid-modified acrylate, anhydride-modified acrylate, ethylene vinyl acetate, acid/acrylate-modified ethylene vinyl acetate, anhydride-modified ethylene vinyl acetate, or a combination thereof.
16. The process of claim 13, wherein the polar polymer layer is selected from the group consisting of nylon, polyester, ethylene vinyl alcohol, a copolymer of nylon, a copolymer of polyester, a copolymer of ethylene vinyl alcohol, and a combination thereof.
17. The process of claim 12 wherein the nonwoven material is attached to at least the portion of either the first non-cavitated skin layer or the second non-cavitated skin layer without an adhesive.
18. The process of claim 17 wherein the nonwoven material is attached to at least the portion of either the first non-cavitated skin layer or the second non-cavitated skin layer via ultrasonic welding.
19. The process of claim 1 wherein the MD stretching and the CD-IMG stretching occur in a separate manufacturing process that is not in-line with formation of the quenched film.
20. The process of claim 13 wherein the MD stretching and the CD-IMG stretching occur in a separate manufacturing process that is not in-line with formation of the quenched film.
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AU2016350820B2 (en) 2020-06-18
ECSP18042587A (en) 2018-08-31
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KR20180083871A (en) 2018-07-23

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